U.S. patent application number 16/107069 was filed with the patent office on 2019-01-24 for vapor disposition of silicon-containing films using penta-substituted disilanes.
The applicant listed for this patent is L'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des Procedes Georges Claude. Invention is credited to Julien Gatineau, Jean-Marc Girard, Changhee Ko, Yann Martelat, Naoto Noda, Shingo Okubo, Ivan Oshchepkov, Kazutaka Yanagita.
Application Number | 20190027357 16/107069 |
Document ID | / |
Family ID | 55749599 |
Filed Date | 2019-01-24 |
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United States Patent
Application |
20190027357 |
Kind Code |
A1 |
Girard; Jean-Marc ; et
al. |
January 24, 2019 |
VAPOR DISPOSITION OF SILICON-CONTAINING FILMS USING
PENTA-SUBSTITUTED DISILANES
Abstract
Disclosed are methods of depositing silicon-containing films on
one or more substrates via vapor deposition processes using
penta-substituted disilanes, such as pentahalodisilane or
pentakis(dimethylamino)disilane.
Inventors: |
Girard; Jean-Marc;
(Versailles, FR) ; Ko; Changhee; (Tsukuba, JP)
; Oshchepkov; Ivan; (Tsukuba, JP) ; Yanagita;
Kazutaka; (Tsukuba, JP) ; Okubo; Shingo;
(Tsukuba, JP) ; Noda; Naoto; (Tsukuba, JP)
; Gatineau; Julien; (San Jose, CA) ; Martelat;
Yann; (Bear, DE) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
L'Air Liquide, Societe Anonyme pour l'Etude et l'Exploitation des
Procedes Georges Claude |
Paris |
|
FR |
|
|
Family ID: |
55749599 |
Appl. No.: |
16/107069 |
Filed: |
August 21, 2018 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
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15459158 |
Mar 15, 2017 |
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16107069 |
|
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14979816 |
Dec 28, 2015 |
9633838 |
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15459158 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
C23C 16/345 20130101;
H01L 21/02532 20130101; H01L 21/02274 20130101; H01L 21/0228
20130101; H01L 21/0217 20130101; H01L 21/02211 20130101; H01L
21/02529 20130101; C23C 16/36 20130101; H01L 21/02247 20130101;
C23C 16/24 20130101; H01L 21/02208 20130101; H01L 21/02236
20130101; H01L 21/02167 20130101; C23C 16/45553 20130101; H01L
21/02271 20130101; H01L 21/0262 20130101; H01L 21/02164 20130101;
H01L 21/02277 20130101; C23C 16/325 20130101; H01L 21/32055
20130101; C23C 16/402 20130101 |
International
Class: |
H01L 21/02 20060101
H01L021/02; C23C 16/24 20060101 C23C016/24; C23C 16/455 20060101
C23C016/455; C23C 16/40 20060101 C23C016/40; C23C 16/36 20060101
C23C016/36; C23C 16/34 20060101 C23C016/34; C23C 16/32 20060101
C23C016/32 |
Claims
1. A thermal vapor deposition method of depositing a silicon film
on a substrate, the method comprising: a) setting a reactor
containing the substrate to a temperature ranging from
approximately 550.degree. C. to approximately 800.degree. C. and a
pressure ranging from approximately 0.1 to approximately 100 Torr
(13 Pa to 13,332 Pa); b) introducing a vapor of pentachlorodisilane
into the reaction chamber to form the silicon film on the
substrate.
2. The method of claim 1, further comprising introducing an inert
gas.
3. The method of claim 2, wherein the inert gas is N.sub.2.
4. The method of claim 1, further comprising introducing a reducing
gas.
5. The method of claim 1, wherein the silicon film contains between
approximately 0 atomic % and 5 atomic % C; between approximately 0
atomic % and 1 atomic % N; and between approximately 0 atomic % and
1 atomic % Cl.
6. The method of claim 5, wherein the silicon film is an amorphous
silicon film.
7. The method of claim 5, wherein the silicon film is a polysilicon
film.
8. The method of claim 3, wherein the silicon film contains between
approximately 0 atomic % and 5 atomic % C; between approximately 0
atomic % and 1 atomic % N; and between approximately 0 atomic % and
1 atomic % Cl.
9. The method of claim 8, wherein the silicon film is an amorphous
silicon film.
10. The method of claim 8, wherein the silicon film is a
polysilicon film.
Description
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application is a divisional of U.S. patent application
Ser. No. 15/459,158, filed Mar. 15, 2017, which is a divisional of
U.S. patent application Ser. No. 14/979,816, filed Dec. 28, 2015
and matured to grant as U.S. Pat. No. 9,633,838, the entire
contents of which are incorporated herein by reference.
TECHNICAL FIELD
[0002] Disclosed are methods of depositing silicon-containing films
on one or more substrates via vapor deposition processes using
penta-substituted disilanes, such as pentachlorodisilane or
pentakis(dimethylamino)disilane.
BACKGROUND
[0003] Silicon-containing films are one of the most important
components in semiconductor devices and development of their
various fabrication processes has been highly investigated. Silicon
oxide (SiO.sub.2) films may be used as capacitor and insulating
layers. D. Tahir et al., "Electronic and optical properties of
Al.sub.2O.sub.3/SiO.sub.2 films grown on Si substrate", J. Phys. D:
Appl. Phys. 43, 255301 (2010). Silicon nitride (SiN), silicon
carbide (SiC) and silicon carbonitride (SiCN) films may be used as
hard mask, diffusion barriers or trench etch-stop layers. Si-Yi Li
et al., "Selectivity Control in Plasma Etching for Dual Damascene
with OSG films", Abstract #242, 199.sup.th ECS Meeting (2001); Ping
Xu et al., "A Breakthrough in Low-k Barrier/Etch Stop Films for
Copper Damascene Applications", Semiconductor FABTECH, 11, 239
(2000); Y. L. Wang et al., "Integration of SiCN as a Low k Etch
Stop and Cu Passivation in a High Performance Cu/Low k
Interconnect", Materials 5, 377-384 (2012).
[0004] Use of pentachlorodisilane (PCDS or Si.sub.2HCl.sub.5) and
pentakis(dimethylamino)disilane (Si.sub.2H(NMe.sub.2).sub.5) as
vapor deposition precursors has been described in the prior art.
See, e.g., US2004/224089 to Singh et al., WO2007/112780 to
Dussarrat, and US2008/026149 to Tomasini et al.
[0005] However, it remains a challenge to find silicon-containing
precursors suitable for commercial deposition of silicon-containing
films.
SUMMARY
[0006] Disclosed are vapor deposition processes for the deposition
of silicon-containing films on substrates. The vapor of a
Si-containing film forming precursor is introduced into a reactor
containing the substrate. The Si-containing film forming
composition comprises a penta-substituted disilane precursor. At
least part of the penta-substituted disilane film forming
precursors is deposited onto the substrate to form the
silicon-containing film. The disclosed processes may further
include one or more of the following aspects: [0007] The
penta-substituted disilane precursor being pentachlorodisilane
(PCDS or Si.sub.2HCl.sub.5); [0008] The penta-substituted disilane
precursor being pentaiododisilane (Si.sub.2HI.sub.5); [0009] The
penta-substituted disilane precursor being pentabromodisilane
(Si.sub.2HBr.sub.5); [0010] The penta-substituted disilane
precursor being pentafluorodisilane (Si.sub.2HF.sub.5); [0011] The
penta-substituted disilane precursor being
pentakis(dimethylamino)disilane [Si.sub.2H(NMe.sub.2).sub.5];
[0012] the Si-containing film forming composition comprising
between approximately 99% w/w and approximately 100% w/w of the
penta-substituted disilane precursor; [0013] the Si-containing film
forming composition comprising between approximately 95% w/w and
approximately 100% w/w of the penta-substituted disilane precursor;
[0014] the Si-containing film forming composition comprising
between approximately 0% w/w and approximately 5% w/w impurities;
[0015] the Si-containing film forming composition comprising
between approximately 0.0% w/w and approximately 2.0% w/w
impurities; [0016] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w impurities; [0017] the impurities including hexa-, tetra-, and
tris-substituted disilanes having the formula
Si.sub.2H.sub.xX.sub.y, wherein X.dbd.Cl, Br, I, or NR.sub.2,
R.dbd.H or a C1-C4 alkyl group, x=0, 2, or 3, and x+y=6;
tetra-substituted silanes having the formula SiX.sub.4, wherein
X.dbd.Cl, Br, I, or NR.sub.2, and R.dbd.H or a C1-C4 alkyl group;
tris-substituted silanes having the formula SiHX.sub.3, wherein
X.dbd.Cl, Br, I, or NR.sub.2, and R.dbd.H or a C1-C4 alkyl group;
partially substituted trisilanes having the formula
Si.sub.3H.sub.xX.sub.y, wherein X.dbd.Cl, Br, I, or NR.sub.2,
R.dbd.H or a C1-C4 alkyl group, x+y=8 and x=1 to 6; siloxanes
having the formula SiHX2--O--SiX.sub.3, wherein X.dbd.Cl, Br, I, or
NR.sub.2, and R.dbd.H or a C1-C4 alkyl group; siloxanes having the
formula H.sub.xX.sub.ySi--O--SiH.sub.xX.sub.y, wherein X.dbd.Cl,
Br, I, or NR.sub.2, R.dbd.H or a C1-C4 alkyl group, x=0, 2, or 3,
and x+y=3; siloxanes having the formula
SiH.sub.xX.sub.y--O--SiH.sub.xX.sub.y, wherein X.dbd.Cl, Br, I, or
NR.sub.2, R.dbd.H or a C1-C4 alkyl group hydrogen, x+y=3, and x=0
or 1; siloxanes having the formula
H.sub.xX.sub.ySi--O--(Si.sub.2H.sub.aX.sub.b), wherein X.dbd.Cl,
Br, I, or NR.sub.2, R.dbd.H or a C1-C4 alkyl group, x+y=3, a+b=6,
x=1 to 3, and a=0, 2, or 3; siloxanes having the formula
H.sub.xX.sub.ySi--O--SiH.sub.aX.sub.b--O--SiH.sub.xX.sub.y, wherein
X.dbd.Cl, Br, I, or NR.sub.2, R.dbd.H or a C1-C4 alkyl group,
x+y=3, a+b=2, x=1 to 3, and a=0 to 2; iodine; bromine; chlorine;
dialkylamines, such as dimethylamine or ethylamine; THF; ether;
pentane; hexane; cyclohexane; heptanes; benzene; toluene; or
combinations thereof; [0018] the Si-containing film forming
composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w hexa-substituted disilanes having the
formula Si.sub.2X.sub.6, wherein X.dbd.Cl, Br, I, or NR.sub.2,
R.dbd.H or a C1-C4 alkyl group; [0019] the Si-containing film
forming composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w tetra-substituted disilanes having the
formula Si.sub.2H.sub.2X.sub.4, wherein X.dbd.Cl, Br, I, or
NR.sub.2, R.dbd.H or a C1-C4 alkyl group; [0020] the Si-containing
film forming composition comprising between approximately 0.0% w/w
and approximately 1.0% w/w tris-substituted disilanes having the
formula Si.sub.2H.sub.3X.sub.3, wherein X.dbd.Cl, Br, I, or
NR.sub.2, R.dbd.H or a C1-C4 alkyl group; [0021] the Si-containing
film forming composition comprising between approximately 0.0% w/w
and approximately 1.0% w/w tetra-substituted silanes having the
formula SiX.sub.4, wherein X.dbd.Cl, Br, I, or NR.sub.2, and
R.dbd.H or a C1-C4 alkyl group; [0022] the Si-containing film
forming composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w tris-substituted silanes having the formula
SiHX.sub.3, wherein X.dbd.Cl, Br, I, or NR.sub.2, and R.dbd.H or a
C1-C4 alkyl group; [0023] the Si-containing film forming
composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w partially substituted trisilanes having the
formula Si.sub.3H.sub.xX.sub.y, wherein X.dbd.Cl, Br, I, or
NR.sub.2, R.dbd.H or a C1-C4 alkyl group, x+y=8, and x=1 to 6;
[0024] the Si-containing film forming composition comprising
between approximately 0.0% w/w and approximately 1.0% w/w siloxanes
having the formula SiHX.sub.2--O--SiX.sub.3, wherein X.dbd.Cl, Br,
I, or NR.sub.2, and R.dbd.H or a C1-C4 alkyl group; [0025] the
Si-containing film forming composition comprising between
approximately 0.0% w/w and approximately 1.0% w/w siloxanes having
the formula H.sub.xX.sub.ySi--O--SiH.sub.xX.sub.y, wherein
X.dbd.Cl, Br, I, or NR.sub.2, R.dbd.H or a C1-C4 alkyl group, x=0,
2, or 3, and x+y=3; [0026] the Si-containing film forming
composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w siloxanes having the formula
SiH.sub.xX.sub.y--O--SiH.sub.xX.sub.y, wherein X.dbd.Cl, Br, I, or
NR.sub.2, R.dbd.H or a C1-C4 alkyl group hydrogen, x+y=3, and x=0
or 1; [0027] the Si-containing film forming composition comprising
between approximately 0.0% w/w and approximately 1.0% w/w siloxanes
having the formula H.sub.xX.sub.ySi--O--(Si.sub.2H.sub.aX.sub.b),
wherein X.dbd.Cl, Br, I, or NR.sub.2, R.dbd.H or a C1-C4 alkyl
group, x+y=3, a+b=5, x=1 to 3, and a=0, 2, or 3; [0028] the
Si-containing film forming composition comprising between
approximately 0.0% w/w and approximately 1.0% w/w siloxanes having
the formla
H.sub.xX.sub.ySi--O--SiH.sub.aX.sub.b--O--SiH.sub.xX.sub.y, wherein
X.dbd.Cl, Br, I, or NR.sub.2, R.dbd.H or a C1-C4 alkyl group,
x+y=3, a+b=2, x=1 to 3, and a=0 to 2; [0029] the Si-containing film
forming composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w dialkylamines, such as dimethylamine or
ethylamine; [0030] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w THF; [0031] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w ether; [0032] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w pentane; [0033] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w hexane; [0034] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w cyclohexane; [0035] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w heptanes; [0036] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w benzene; [0037] the Si-containing film forming composition
comprising between approximately 0.0% w/w and approximately 1.0%
w/w toluene; [0038] the Si-containing film forming composition
comprising between approximately 0 ppbw and approximately 1 ppmw
metal impurities; [0039] the Si-containing film forming composition
comprising between approximately 0 ppbw and approximately 500 ppbw
metal impurities; [0040] The vapor deposition process being an
atomic layer deposition (ALD) process; [0041] The vapor deposition
process being a chemical vapor deposition (CVD) process; [0042]
Further comprising introducing an oxidant into the reactor; [0043]
The oxidant being O.sub.2, O.sub.3, H.sub.2O, H.sub.2O.sub.2, NO,
N.sub.2O, NO.sub.2, carboxylic acids, formic acid, acetic acid,
propionic acid, oxygen containing radicals thereof, or mixtures
thereof; [0044] The oxidant being O.sub.2, O.sub.3, H.sub.2O,
oxygen containing radicals thereof, or mixtures thereof; [0045] The
oxidant being O.sub.2, O.sub.3, oxygen containing radicals thereof,
or mixtures thereof; [0046] The oxidant being a 7.2% v/v mixture of
O.sub.3in O.sub.2; [0047] The silicon-containing film being silicon
oxide; [0048] The silicon oxide film having a wet etch rate less
than or equal to ten times the wet etch rate of silicon oxide
deposited by thermal deposition using a dilute HF solution (0.5 to
1% HF); [0049] The silicon oxide film being deposited at a
temperature ranging from approximately 450.degree. C. to
approximately 800.degree. C.; [0050] The ALD process depositing a
silicon oxide film at a temperature ranging from approximately
550.degree. C. to approximately 600.degree. C.; [0051] The thermal
ALD process depositing a silicon oxide film at a temperature
ranging from approximately 100.degree. C. to approximately
400.degree. C.; [0052] The plasma ALD process depositing a silicon
oxide film at a temperature ranging from approximately room
temperature to approximately 400.degree. C.; [0053] The silicon
oxide film containing between approximately 0 atomic % and
approximately 5 atomic % carbon; [0054] The silicon oxide film
containing between approximately 0 atomic % and approximately 2.5
atomic % carbon; [0055] The silicon oxide film containing between
approximately 0 atomic % and approximately 1 atomic % carbon;
[0056] The silicon oxide film containing between approximately 0
atomic % and approximately 1 atomic % nitrogen; [0057] The silicon
oxide film containing between approximately 0 atomic % and
approximately 1 atomic % chlorine; [0058] Silicon oxide film
exhibiting step coverage between approximately 70% and
approximately 100% for an aspect ratio of 1:7; [0059] Silicon oxide
film exhibiting step coverage between approximately 70% and
approximately 100% for an aspect ratio of 1:20; [0060] Silicon
oxide film exhibiting step coverage between approximately 90% and
approximately 100% for an aspect ratio of 1:7; [0061] Silicon oxide
film exhibiting step coverage between approximately 90% and
approximately 100% for an aspect ratio of 1:20; [0062] Further
comprising introducing a nitrogen-containing reactant into the
reactor; [0063] The nitrogen-containing reactant being NH.sub.3,
N.sub.2H.sub.4, N(SiH.sub.3).sub.3, N(CH.sub.3)H.sub.2,
N(C.sub.2H.sub.5)H.sub.2, N(CH.sub.3).sub.2H,
N(C.sub.2H.sub.5).sub.2H, N(CH.sub.3).sub.3,
N(C.sub.2H.sub.5).sub.3, (SiMe.sub.3).sub.2NH,
(CH.sub.3)HNNH.sub.2, (CH.sub.3).sub.2NNH.sub.2,
nitrogen-containing radical species thereof, and mixtures thereof;
[0064] The nitrogen-containing reactant being NH.sub.3; [0065] The
silicon-containing film being silicon nitride; [0066] The silicon
nitride film being deposited at a temperature ranging from
approximately 450.degree. C. to approximately 650.degree. C.;
[0067] The silicon nitride film having a refractivity index that
ranges from approximately 1.7 to approximately 2.2; [0068] Further
comprising introducing an amine, an alkylaminosilane, or a
disilazane into the reactor; [0069] The amine being ammonia; [0070]
The alkylaminosilane being bis(diethylamino)silane; [0071] The
alkylaminosilane being tris(dimethylamino)silane; [0072] The
disilazane being hexamethyldisilazane; [0073] The silicon
containing film being a carbon doped silicon nitride film; [0074]
The carbon doped silicon nitride film having a carbon concentration
ranging from approximately 5 atomic % to approximately 40 atomic %;
[0075] The carbon doped silicon nitride film having a nitrogen
concentration ranging from approximately 20 atomic % to
approximately 60 atomic %; [0076] The carbon doped silicon nitride
film having an oxygen concentration ranging from approximately 0
atomic % to approximately 5 atomic %; [0077] The process being a
plasma enhanced atomic layer deposition (PEALD) process; [0078]
Further comprising introducing a nitrogen-containing reactant into
the reactor; [0079] The nitrogen-containing reactant being N.sub.2,
NH.sub.3, N.sub.2H.sub.4, N(SiH.sub.3).sub.3, N(CH.sub.3)H.sub.2,
N(C.sub.2H.sub.5)H.sub.2, N(CH.sub.3).sub.2H,
N(C.sub.2H.sub.5).sub.2H, N(CH.sub.3).sub.3,
N(C.sub.2H.sub.5).sub.3, (SiMe.sub.3).sub.2NH,
(CH.sub.3)HNNH.sub.2, (CH.sub.3).sub.2NNH.sub.2, a mixture of
N.sub.2 and H.sub.2, nitrogen-containing radical species thereof,
and mixtures thereof; [0080] The nitrogen-containing reactant being
NH.sub.3, N.sub.2, a mixture of N.sub.2 and H.sub.2, and mixtures
thereof; [0081] The mixture of N.sub.2 and H.sub.2 containing
between approximately 0% v/v to approximately 70% v/v H.sub.2;
[0082] The mixture of N.sub.2 and H.sub.2 containing approximately
50% v/v H.sub.2; [0083] The silicon containing film being a carbon
doped silicon nitride film; [0084] The PEALD process depositing a
carbon doped silicon nitride film at a temperature ranging from
approximately 100.degree. C. to approximately 350.degree. C.;
[0085] The carbon doped silicon nitride film having a refractive
index ranging from approximately 1.6 to approximately 2.1; and
[0086] The carbon doped silicon nitride film having a carbon
concentration ranging from approximately 1 atomic % to
approximately 15 atomic %.
[0087] Also disclosed are processes for the vapor deposition of
silicon carbide films on one or more substrates. The vapor of a
silicon-containing film forming composition comprising is
introduced into a reactor containing the substrate(s). The
silicon-containing film forming compositions comprises a silicon
halide. At least part of the silicon halide is deposited onto the
substrate(s) to form the silicon carbide film. An alkyl substituted
metal or metalloid is introduced into the reactor. At least part of
the alkyl substituted metal or metalloid is deposited onto the
substrate to form the silicon carbide film. The disclosed processes
may further include one or more of the following aspects: [0088]
the Si-containing film forming composition comprising between
approximately 99% w/w and approximately 100% w/w of the silicon
halide; [0089] the Si-containing film forming composition
comprising between approximately 95% w/w and approximately 100% w/w
of the silicon halide; [0090] the Si-containing film forming
composition comprising between approximately 0% w/w and
approximately 5% w/w impurities; [0091] the Si-containing film
forming composition comprising between approximately 0.0% w/w and
approximately 2.0% w/w impurities; [0092] the Si-containing film
forming composition comprising between approximately 0.0% w/w and
approximately 1.0% w/w impurities; [0093] the impurities including
hexa-substituted disilanes; alkylamines; dialkylamines;
alkylimines; iodosilanes; aminosilanes; lithium, sodium, or
potassium iodide; iodine; THF; ether; pentane; cyclohexane;
heptanes; benzene; toluene; halogenated metal compounds; [0094] the
Si-containing film forming composition comprising between
approximately 0 ppbw and approximately 1 ppmw metal impurities;
[0095] the Si-containing film forming composition comprising
between approximately 0 ppbw and approximately 500 ppbw metal
impurities; [0096] The silicon halide containing at least one
halogen atom; [0097] The silicon halide containing at least one
silicon-halogen bond; [0098] The silicon halide having the formula
SiX.sub.4, each X independently being Cl, Br, I, H, or R and R
being an aliphatic group; [0099] The silicon halide being
SiCl.sub.3H; [0100] The silicon halide being SiH.sub.2Cl.sub.2;
[0101] The silicon halide being SiH.sub.3Cl; [0102] The silicon
halide being SiI.sub.2H.sub.2; [0103] The silicon halide being
SiHMeI.sub.2; [0104] The silicon halide being SiMe.sub.2I.sub.2;
[0105] The silicon halide being SiH.sub.xCl.sub.3-x(CH.sub.2Cl),
with x=0-3; [0106] The silicon halide being SiH.sub.3(CH.sub.2Cl);
[0107] The silicon halide being SiH.sub.2Cl(CH.sub.2Cl); [0108] The
silicon halide being SiHCl.sub.2(CH.sub.2Cl); [0109] The silicon
halide being SiCl.sub.3(CH.sub.2Cl); [0110] The silicon halide
having the formula Si.sub.2X.sub.6, with each X independently being
Cl, Br, I, or H; [0111] The silicon halide being
pentachlorodisilane; [0112] The silicon halide being
pentabromodisilane; [0113] The silicon halide being
pentaiododisilane; [0114] The silicon halide being
pentafluorodisilane; [0115] The silicon halide being
hexachlorodisilane; [0116] The silicon halide being
hexaiododisilane; [0117] The silicon halide being
monochlorodisilane; [0118] The silicon halide being
monobromodisilane; [0119] The silicon halide being
monoiododisilane; [0120] The silicon halide being
1,1-dichlorodisilane [Cl.sub.2HSi--SiH.sub.3]; [0121] The silicon
halide being dibromodisilane [H.sub.2BrSi--SiBrH.sub.2]; [0122] The
silicon halide being diiododisilane [H.sub.2ISi--SiIH.sub.2];
[0123] The silicon halide being dichlorodisilane
[H.sub.3Si--SiHCl.sub.2]; [0124] The silicon halide being
dibromodisilane [H.sub.3Si--SiHBr.sub.2]; [0125] The silicon halide
being diiododisilane [H.sub.3Si--SiHI.sub.2]; [0126] The silicon
halide having the formula X.sub.3Si--CH.sub.2--SiX.sub.3, with each
X independently being Cl, Br, I, or H; [0127] The silicon halide
being bis(dichlorosilyl)methane [(SiCIH.sub.2).sub.2CH.sub.2];
[0128] The silicon halide being monochlorotrisilapentane
[H.sub.3Si--CH.sub.2--SiH.sub.2Cl]; [0129] The silicon halide
having the formula X.sub.3Si--CH.sub.2--CH.sub.2--SiX.sub.3, with
each X independently being Cl, Br, I, or H; [0130] The silicon
halide having the formula
X.sub.3Si--CH.sub.2--SiX.sub.2--CH.sub.2--SiX.sub.3, with each X
independently being Cl or H, provided at least one terminal X is
Cl; [0131] The silicon halide having the formula
Cl.sub.3Si--CH.sub.2--SiCl.sub.2--CH.sub.2--SiCl.sub.3; [0132] The
silicon halide having the formula
H.sub.3Si--CH.sub.2--SiH.sub.2--CH.sub.2--SiClH.sub.2; [0133] The
silicon halide having the formula (--SiX.sub.2--CH.sub.2--).sub.3,
with each X independently being Cl, Br, or I; [0134] The silicon
halide having the formula (--SiHX--CH.sub.2--).sub.3, with each X
independently being Cl, Br, or I; [0135] The silicon halide being
octachlorotrisilane (OCTS); [0136] The silicon halide being
decachlorotetrasilane (Si.sub.4Cl.sub.10); [0137] The silicon
halide being dodecachloropentasilane (DCPS or Si.sub.5Cl.sub.12);
[0138] The alkyl substituted metal or metalloid having the formula
AlR.sub.3, with each R independently being H, Me, Et, nPr, iPr,
nBu, iBu, or NR.sub.2, provided that when R.sub.3.dbd.H.sub.3 that
the molecule may be adducted with an amine or borohydride; [0139]
The alkyl substituted metal or metalloid being triethyl aluminum;
[0140] The alkyl substituted metal or metalloid being trimethyl
aluminum; [0141] The alkyl substituted metal or metalloid being
AlH.sub.3.NH.sub.3; [0142] The alkyl substituted metal or metalloid
having the formula BR.sub.3, with each R independently being an
alkyl or an allyl group; [0143] The alkyl substituted metal or
metalloid being triethyl boron; [0144] The alkyl substituted metal
or metalloid being trimethyl boron; [0145] The alkyl substituted
metal or metalloid having the formula AlClR.sub.2, with each R
independently being H, Me, Et, nPr, iPr, nBu, or iBu, or NR.sub.2;
[0146] The alkyl substituted metal or metalloid having the formula
BXR.sub.2, with X being Cl, Br, or I and each R independently being
an alkyl or an allyl group; [0147] The alkyl substituted metal or
metalloid having the formula ZnR.sub.2, with each R independently
being Me, Et, nPr, iPr, nBu, or iBu; [0148] The alkyl substituted
metal or metalloid having the formula GaR.sub.3, with each R
independently being Me, Et, nPr, iPr, nBu, iBu, or NR.sub.2; [0149]
The alkyl substituted metal or metalloid being trimethyl gallium;
and [0150] The alkyl substituted metal or metalloid having the
formula InR.sub.3, with each R independently being Me, Et, nPr,
iPr, nBu, iBu, or NR.sub.2.
[0151] Also disclosed is a Si-containing film forming composition
delivery device comprising a canister having an inlet conduit and
an outlet conduit and containing any of the Si-containing film
forming compositions disclosed above. The disclosed device may
include one or more of the following aspects: [0152] the
Si-containing film forming composition having a total concentration
of metal contaminants of less than 10 ppmw; [0153] an end of the
inlet conduit end located above a surface of the Si-containing film
forming composition and an end of the outlet conduit located below
the surface of the Si-containing film forming composition; [0154]
an end of the inlet conduit end located below a surface of the
Si-containing film forming composition and an end of the outlet
conduit located above the surface of the Si-containing film forming
composition; [0155] further comprising a diaphragm valve on the
inlet and the outlet; [0156] further comprising one or more barrier
layers on an interior surface of the canister; [0157] further
comprising one to four barrier layers on an interior surface of the
canister; [0158] further comprising one or two barrier layers on an
interior surface of the canister; [0159] each barrier layer
comprising a silicon oxide layer, a silicon nitride layer, silicon
oxynitride layer, a silicon carbonitride, silicon oxycarbonitride
layer, or combinations thereof; [0160] wherein each barrier layer
is 5 to 1000 nm in thickness; [0161] wherein each barrier layer is
50 to 500 nm in thickness; [0162] the Si-containing film forming
composition comprising pentachlorodisilane (PCDS or
Si.sub.2HCl.sub.5); [0163] the Si-containing film forming
composition comprising pentaiododisilane (Si.sub.2HI.sub.5); [0164]
the Si-containing film forming composition comprising
pentabromodisilane (Si.sub.2HBr.sub.5); [0165] the Si-containing
film forming composition comprising pentafluorodisilane
(Si.sub.2HF.sub.5); [0166] the Si-containing film forming
composition comprising pentakis(dimethylamino)disilane
[Si.sub.2H(NMe.sub.2).sub.5]; [0167] The Si-containing film forming
composition comprising SiCl.sub.3H; [0168] The Si-containing film
forming composition comprising SiH.sub.2Cl.sub.2; [0169] The
Si-containing film forming composition comprising SiH.sub.3Cl;
[0170] The Si-containing film forming composition comprising
SiI.sub.2H.sub.2; [0171] The Si-containing film forming composition
comprising SiHMeI.sub.2; [0172] The Si-containing film forming
composition comprising SiMe.sub.2I.sub.2; [0173] The Si-containing
film forming composition comprising
SiH.sub.xCl.sub.3-x(CH.sub.2Cl), with x=0-3; [0174] The
Si-containing film forming composition comprising
SiH.sub.3(CH.sub.2Cl); [0175] The Si-containing film forming
composition comprising SiH.sub.2Cl(CH.sub.2Cl); [0176] The
Si-containing film forming composition comprising
SiHCl.sub.2(CH.sub.2Cl); [0177] The Si-containing film forming
composition comprising SiCl.sub.3(CH.sub.2Cl); [0178] The
Si-containing film forming composition comprising a silicon halide
having the formula Si.sub.2X.sub.6, with each X independently being
Cl, Br, I, or H; [0179] The Si-containing film forming composition
comprising pentachlorodisilane; [0180] The Si-containing film
forming composition comprising pentabromodisilane; [0181] The
Si-containing film forming composition comprising
pentaiododisilane; [0182] The Si-containing film forming
composition comprising pentafluorodisilane; [0183] The
Si-containing film forming composition comprising
hexachlorodisilane; [0184] The Si-containing film forming
composition comprising hexaiododisilane; [0185] The Si-containing
film forming composition comprising monochlorodisilane; [0186] The
Si-containing film forming composition comprising
monobromodisilane; [0187] The Si-containing film forming
composition comprising monoiododisilane; [0188] The Si-containing
film forming composition comprising 1,1-dichlorodisilane
[Cl.sub.2HSi--SiH.sub.3]; [0189] The Si-containing film forming
composition comprising dibromodisilane [H.sub.2BrSi--SiBrH.sub.2];
[0190] The Si-containing film forming composition comprising
diiododisilane [H.sub.2ISi--SiIH.sub.2]; [0191] The Si-containing
film forming composition comprising dichlorodisilane
[H.sub.3Si--SiHCl.sub.2]; [0192] The Si-containing film forming
composition comprising dibromodisilane [H.sub.3Si--SiHBr.sub.2];
[0193] The Si-containing film forming composition comprising
diiododisilane [H.sub.3Si--SiHI.sub.2]; [0194] The Si-containing
film forming composition comprising a silicon halide having the
formula X.sub.3Si--CH.sub.2--SiX.sub.3, with each X independently
being Cl, Br, I, or H; [0195] The Si-containing film forming
composition comprising bis(dichlorosilyl)methane
[(SiClH.sub.2).sub.2CH.sub.2]; [0196] The Si-containing film
forming composition comprising monochlorotrisilapentane
[H.sub.3Si--CH.sub.2--SiH.sub.2Cl]; [0197] The Si-containing film
forming composition comprising a halide having the formula
X.sub.3Si--CH.sub.2--CH.sub.2--SiX.sub.3, with each X independently
being Cl, Br, I, or H; [0198] The Si-containing film forming
composition comprising a silicon halide having the formula
X.sub.3Si--CH.sub.2--SiX.sub.2--CH.sub.2--SiX.sub.3, with each X
independently being Cl or H, provided at least one terminal X is
Cl; [0199] The Si-containing film forming composition comprising a
silicon halide having the formula
Cl.sub.3Si--CH.sub.2--SiCl.sub.2--CH.sub.2--SiCl.sub.3; [0200] The
Si-containing film forming composition comprising a silicon halide
having the formula
H.sub.3Si--CH.sub.2--SiH.sub.2--CH.sub.2--SiClH.sub.2; [0201] The
Si-containing film forming composition comprising a silicon halide
having the formula (--SiX.sub.2--CH.sub.2--).sub.3, with each X
independently being Cl, Br, or I; [0202] The Si-containing film
forming composition comprising a silicon halide having the formula
(--SiHX--CH.sub.2--).sub.3, with each X independently being Cl, Br,
or I; [0203] The Si-containing film forming composition comprising
octachlorotrisilane (OCTS); [0204] The Si-containing film forming
composition comprising decachlorotetrasilane (Si.sub.4Cl.sub.10);
and [0205] The Si-containing film forming composition comprising
dodecachloropentasilane (DCPS or Si.sub.5Cl.sub.12).
NOTATION AND NOMENCLATURE
[0206] Certain abbreviations, symbols, and terms are used
throughout the following description and claims, and include:
[0207] As used herein, the indefinite article "a" or "an" means one
or more.
[0208] As used herein, the terms "approximately" or "about" mean
.+-.10% of the value stated.
[0209] As used herein, the term "independently" when used in the
context of describing R groups should be understood to denote that
the subject R group is not only independently selected relative to
other R groups bearing the same or different subscripts or
superscripts, but is also independently selected relative to any
additional species of that same R group. For example in the formula
MR.sup.1.sub.x (NR.sup.2R.sup.3).sub.(4-x), where x is 2 or 3, the
two or three R.sup.1 groups may, but need not be identical to each
other or to R.sup.2 or to R.sup.3. Further, it should be understood
that unless specifically stated otherwise, values of R groups are
independent of each other when used in different formulas.
[0210] As used herein, the term "alkyl group" refers to saturated
functional groups containing exclusively carbon and hydrogen atoms.
Further, the term "alkyl group" refers to linear, branched, or
cyclic alkyl groups. Examples of linear alkyl groups include
without limitation, methyl groups, ethyl groups, propyl groups,
butyl groups, etc. Examples of branched alkyls groups include
without limitation, t-butyl. Examples of cyclic alkyl groups
include without limitation, cyclopropyl groups, cyclopentyl groups,
cyclohexyl groups, etc.
[0211] As used herein, the abbreviation, "Me," refers to a methyl
group; the abbreviation, "Et," refers to an ethyl group; the
abbreviation, "Pr," refers to a propyl group; the abbreviation,
"iPr," refers to an isopropyl group; the abbreviation "Bu" refers
to butyl; the abbreviation "tBu" refers to tert-butyl; and the
abbreviation "sBu" refers to sec-butyl.
[0212] Please note that the films or layers deposited, such as
silicon oxide or silicon nitride, may be listed throughout the
specification and claims without reference to their proper
stoichiometry (i.e., SiO.sub.2, SiO.sub.3, Si.sub.3N.sub.4). The
layers may include pure (Si) layers, carbide (Si.sub.oC.sub.p)
layers, nitride (Si.sub.kN.sub.l) layers, oxide (Si.sub.nO.sub.m)
layers, or mixtures thereof, wherein k, l, m, n, o, and p
inclusively range from 1 to 6. For instance, silicon oxide is
Si.sub.nO.sub.m, wherein n ranges from 0.5 to 1.5 and m ranges from
1.5 to 3.5. More preferably, the silicon oxide layer is SiO.sub.2
or SiO.sub.3. The silicon oxide layer may be a silicon oxide based
dielectric material, such as organic based or silicon oxide based
low-k dielectric materials such as the Black Diamond II or III
material by Applied Materials, Inc. Alternatively, any referenced
silicon-containing layer may be pure silicon. Any
silicon-containing layers may also include dopants, such as B, C,
P, As and/or Ge.
[0213] Any and all ranges recited herein are inclusive of their
endpoints (i.e., x=1 to 4 includes x=1, x=4, and x=any number in
between).
[0214] The standard abbreviations of the elements from the periodic
table of elements are used herein. It should be understood that
elements may be referred to by these abbreviations (e.g., Mn refers
to manganese, Si refers to silicon, C refers to carbon, etc.).
BRIEF DESCRIPTION OF THE FIGURES
[0215] For a further understanding of the nature and objects of the
present invention, reference should be made to the following
detailed description, taken in conjunction with the accompanying
figures wherein:
[0216] FIG. 1 is a side view of one embodiment of the Si-containing
film forming composition delivery device disclosed herein;
[0217] FIG. 2 is a side view of a second embodiment of the
Si-containing film forming composition delivery device disclosed
herein;
[0218] FIG. 3 is a schematic diagram of the vapor deposition
apparatus used for the testing in all of the Examples except
Example 10;
[0219] FIG. 4(a) is a X-ray Photoelectron Spectroscopy (XPS) depth
profile of the Si film resulting from thermal decomposition of PCDS
at approximately 400.degree. C.;
[0220] FIG. 4(b) is a XPS depth profile of the Si film resulting
from thermal decomposition of PCDS at approximately 500.degree.
C.;
[0221] FIG. 4(c) is a XPS depth profile of the Si film resulting
from thermal decomposition of PCDS at approximately 600.degree.
C.;
[0222] FIG. 4(d) is a XPS depth profile of the Si film resulting
from thermal decomposition of PCDS at approximately 700.degree.
C.;
[0223] FIG. 5(a) is a XPS depth profile of the Si film resulting
from thermal decomposition of HCDS at approximately 400.degree.
C.;
[0224] FIG. 5(b) is a XPS depth profile of the Si film resulting
from thermal decomposition of HCDS at approximately 500.degree.
C.;
[0225] FIG. 5(c) is a XPS depth profile of the Si film resulting
from thermal decomposition of HCDS at approximately 600.degree.
C.;
[0226] FIG. 5(d) is a XPS depth profile of the Si film resulting
from thermal decomposition of HCDS at approximately 700.degree.
C.;
[0227] FIG. 6 is a graph of the average ALD deposition rate in
Angstroms/cycle of SiO.sub.2 films deposited using PCDS (circles)
or HCDS (triangles) and ozone versus temperatures ranging from
approximately 500.degree. C. to approximately 700.degree. C.;
[0228] FIG. 7 is a graph of the average ALD growth rate in
Angstroms/cycle of SiO.sub.2 films using PCDS and ozone at
approximately 600.degree. C. (squares) or approximately 550.degree.
C. (diamonds) versus PCDS pulse duration in seconds;
[0229] FIG. 8(a) is a XPS depth profile of the SiO.sub.2 film
resulting from ALD deposition using PCDS and ozone on a Si
substrate at approximately 500.degree. C.;
[0230] FIG. 8(b) is a XPS depth profile of the SiO.sub.2 film
resulting from ALD deposition using PCDS and ozone on a Si
substrate at approximately 600.degree. C.;
[0231] FIG. 8(c) is a XPS depth profile of the SiO.sub.2 film
resulting from ALD deposition using PCDS and ozone on a Si
substrate at approximately 650.degree. C.;
[0232] FIG. 8(d) is a XPS depth profile of the SiO.sub.2 film
resulting from ALD deposition using PCDS and ozone on a Si
substrate at approximately 700.degree. C.;
[0233] FIG. 9 is a scanning electronic microscope (SEM) picture
showing step coverage of an SiO.sub.2 film deposited on a deep hole
pattern wafer having an aspect ratio of 40:1 by 350 ALD cycles
using PCDS and ozone at approximately 600.degree. C.;
[0234] FIG. 9(a) is an enlarged SEM picture showing the SiO.sub.2
step coverage at the top of the structure of FIG. 9;
[0235] FIG. 9(b) is an enlarged SEM picture showing the SiO.sub.2
step coverage at the middle of the structure of FIG. 9;
[0236] FIG. 9(c) is an enlarged SEM picture showing the SiO.sub.2
step coverage at the bottom of the structure of FIG. 9;
[0237] FIG. 10 is a graph of the average ALD deposition rate in
Angstroms/cycle (diamond) and refractive index (square) of
SiO.sub.2 films deposited using PCDS (circles) or HCDS (triangles),
water, and triethylamine versus temperatures ranging from
approximately 50.degree. C. to approximately 100.degree. C.;
[0238] FIG. 11 is a XPS depth profile of the silicon oxide film
resulting from ALD deposition using PCDS, water, and TEA;
[0239] FIG. 12 is a graph of the average CVD deposition rate in
Angstroms/minute (hollow) and refractive index (filled) of SiN
films deposited using PCDS (circle) and HCDS (square) and NH.sub.3
versus temperatures ranging from approximately 450.degree. C. to
approximately 600.degree. C.;
[0240] FIG. 13 is a graph of the average ALD deposition rate in
Angstroms/cycle (hollow) and refractive index (filled) of SiN films
deposited using PCDS (circle), HCDS(square), and
octachlorotrisilane (triangle) and NH3 versus temperature ranging
from approximately 350.degree. C. to approximately 600.degree.
C.;
[0241] FIG. 14 is a XPS depth profile for the SiN film deposited at
600.degree. C. with PCDS and NH.sub.3;
[0242] FIG. 15 is a XPS depth profile of the SiC film resulting
from ALD deposition using PCDS or HCDS and trimethylaluminum at
400.degree. C.;
[0243] FIG. 16 is a graph demonstrating the film thickness and
refractive index versus measurement position;
[0244] FIG. 17 is a schematic diagram of a plasma vapor deposition
apparatus used in Example 10;
[0245] FIG. 18 is a XPS depth profile of the Si(C)N film resulting
from ALD deposition using pentakis(dimethylamino)disilane and
N.sub.2 plasma at 275.degree. C.; and
[0246] FIG. 19 is a graph of the average ALD deposition rate and in
Angstroms/cycle (square) and refractive index (circle) of the
Si(C)N films deposited using pentakis(dimethylamino)disilane and
N.sub.2 plasma versus purge time in seconds.
DESCRIPTION OF PREFERRED EMBODIMENTS
[0247] Processes for the deposition of silicon-containing films on
one or more substrates are disclosed. The vapor of a
silicon-containing film forming composition is introduced into a
reactor having a substrate disposed therein. The silicon-containing
film forming compositions comprises a penta-substituted disilane
precursor. At least part of the penta-substituted disilane
precursor is deposited onto the substrate to form the
silicon-containing film.
[0248] The penta-substituted disilane precursor may be
pentachlorodisilane (PCDS or Si.sub.2HCl.sub.5),
pentafluorodisilane (Si.sub.2HF.sub.5), pentabromodisilane
(Si.sub.2HBr.sub.5), or pentaiododisilane (Si.sub.2HI.sub.5).
[0249] Pentachlorodisilane is not currently commercially available.
However, methods of producing pentachlorodisilane are known in the
art. One preferred method is disclosed in JP Pat App No 2014-194723
filed Sep. 25, 2014, the contents of which are incorporated by
reference herein in its entirety. More particularly, PCDS may be
isolated by distillation from the chlorosilane by-products produced
in the synthesis of trichlorosilane. The corresponding
pentahalodisilanes may be synthesized in the same manner. The
pentahalodisilane may be purified by continuous or fractional batch
distillation to a purity ranging from approximately 95% w/w to
approximately 100% w/w, preferably ranging from approximately 99%
w/w to approximately 100% w/w. One of ordinary skill in the art
will recognize that the distillation column will require a large
number of theoretical plates in order to purify the
pentahalodisilane from its halodisilane analogs.
[0250] The concentration of hexahalodisilane in the purified
pentahalodisilane may range from approximately 0% w/w to
approximately 5% w/w, preferably from approximately 0% w/w to
approximately 1% w/w. The concentration of O.sub.2 in the purified
pentahalodisilane may range from approximately 0 ppmw to
approximately 50 ppmw, preferably from approximately 0 ppmw to
approximately 4 ppmw, and more preferably from approximately 0 ppmw
to approximately 1 ppmw. The purified pentahalodisilane should
contain no water, 0 ppmw, or the two will react. The concentration
of Cr in the purified pentahalodisilane may range from
approximately 0 ppmw to approximately 25 ppmw. The concentration of
Fe in the purified pentahalodisilane may range from approximately 0
ppmw to approximately 100 ppmw. The concentration of Na in the
purified pentahalodisilane may range from approximately 0 ppmw to
approximately 50 ppmw. The concentration of Ni in the purified
pentahalodisilane may range from approximately 0 ppmw and
approximately 25 ppmw.
[0251] Alternatively, the penta-substituted disilane precursor may
be pentakis(dimethylamino)disilane
[PDMADS-Si.sub.2H(NMe.sub.2).sub.5]. PDMADS is also not currently
commercially available. However, methods of synthesizing it are
disclosed, for example, in WO2007/112780 to Dussarrat, the contents
of which are incorporated by reference herein in its entirety. More
particularly, pentakis(dimethyamino)chlorodisilane is produced by
reacting hexachlorodisilane with more than 5 fold moles of
dimethylamine (Me.sub.2NH) in an organic solvent at a temperature
from -30.degree. C. to 50.degree. C. PDMADS is formed by reduction
of the pentakis(dimethylamino)chlorodisilane using lithium aluminum
hydride or sodium boron hydride.
[0252] PDMADS may be purified by continuous or fractional batch
distillation to a purity ranging from approximately 95% w/w to
approximately 100% w/w, preferably ranging from approximately 99%
w/w to approximately 100% w/w. One of ordinary skill in the art
will recognize that the distillation column will require a large
number of theoretical plates in order to purify PDMADS from its
aminodisilane analogs.
[0253] The concentration of hexa(dimethylamino)disilane in the
purified PDMADS may range from approximately 0% w/w to
approximately 5% w/w, preferably from approximately 0% w/w to
approximately 1% w/w. The concentration of O.sub.2 in the purified
PDMADS may range from approximately 0 ppmw to approximately 50
ppmw, preferably from approximately 0 ppmw to approximately 4 ppmw,
and more preferably from approximately 0 ppmw to approximately 1
ppmw. No water (0 ppmw) can be contained within PDMADS or the two
will react. The concentration of Cr in the purified PDMADS may
range from approximately 0 ppmw to approximately 25 ppmw. The
concentration of Fe in the purified PDMADS may range from
approximately 0 ppmw to approximately 100 ppmw. The concentration
of Na in the purified PDMADS may range from approximately 0 ppmw to
approximately 50 ppmw. The concentration of Ni in the purified
PDMADS may range from approximately 0 ppmw and approximately 25
ppmw.
[0254] As illustrated in the following Examples, Applicants have
surprisingly found that using penta-substituted disilane film
forming precursors for the process of silicon-containing film
deposition provides a faster ALD growth rate and a reasonable ALD
temperature window at which useable film is deposited with high
purity when compared to films deposited by analogous
hexasubstituted disilanes, such as HCDS or Si.sub.2(NHMe).sub.6.
Applicants believe that the substitution of one ligand of a
hexasubstituted disilane, wherein all of the ligands are the same,
with H produces a more reactive molecule (i.e.,
Si.sub.2Cl.sub.6.fwdarw.Si.sub.2HCl.sub.5 or
Si.sub.2(NMe.sub.2).sub.6.fwdarw.Si.sub.2H(NMe.sub.2).sub.5). The
increased reactivity of the penta-substituted disilane film forming
precursors may be due to the smaller atomic size of the hydrogen
ligand compared to the larger atomic size of the chlorine or
dimethylamino ligands in case of HCDS and
Si.sub.2(NMe.sub.2).sub.6, respectively. The smaller sized hydrogen
ligand may provide less steric hindrance and therefore a higher
possibility of physi- or chemi-sorption onto the substrate or onto
the previously formed layer, resulting in faster growth behavior.
The hydrogen ligand may also make the penta-substituted disilane
film forming precursors more acidic than HCDS and
Si.sub.2(NMe.sub.2).sub.6, resulting in higher reactivity.
Increased reactivity may also be due to substitution of one ligand
of a hexasubstituted disilane with H, slightly polarizing the
Si--Si bond due to the change from a symmetrical molecule to an
unsymmetrical molecule.
##STR00001##
[0255] The disclosed processes for forming silicon-containing
layers on a substrate using a vapor deposition process may be
useful in the manufacture of semiconductor, photovoltaic, LCD-TFT,
or flat panel type devices. The disclosed Si-containing film
forming compositions may be used to deposit silicon-containing
films using any deposition methods known to those of skill in the
art. Examples of suitable deposition methods include chemical vapor
deposition (CVD) or atomic layer deposition (ALD). Exemplary CVD
methods include thermal CVD, plasma enhanced CVD (PECVD), pulsed
CVD (PCVD), low pressure CVD (LPCVD), sub-atmospheric CVD (SACVD)
or atmospheric pressure CVD (APCVD), hot-wire CVD (HWCVD, also
known as cat-CVD, in which a hot wire serves as an energy source
for the deposition process), radicals incorporated deposition,
super critical fluid deposition, and combinations thereof.
Exemplary ALD methods include thermal ALD, plasma enhanced ALD
(PEALD), spatial isolation ALD, hot-wire ALD (HWALD), and
combinations thereof. The deposition method is preferably ALD,
PE-ALD, or spatial isolation ALD in order to provide suitable step
coverage and film thickness control.
[0256] The disclosed Si-containing film forming compositions may
comprise only the penta-substituted disilane precursor.
Alternatively, the Si-containing film forming composition may
further comprise a solvent, such as toluene, xylene, mesitylene,
decane, dodecane, or other suitable hydrocarbons. The disclosed
precursors may be present in varying concentrations in the
solvent.
[0257] The disclosed Si-containing film forming compositions are
introduced into a reactor in vapor form by conventional means, such
as tubing and/or flow meters. The vapor form of the composition may
be produced through a conventional vaporization step such as direct
vaporization, distillation, or by bubbling. The composition may be
fed in liquid state to a vaporizer (direct liquid injection or
"DLI") where it is vaporized before it is introduced into the
reactor. Alternatively, the composition may be vaporized by passing
a carrier gas into a container containing the composition or by
bubbling the carrier gas into the composition. The carrier gas may
include, but is not limited to, Ar, He, N.sub.2, and mixtures
thereof. Bubbling with a carrier gas may also remove any dissolved
oxygen present in the composition. The carrier gas and composition
are then introduced into the reactor as a vapor.
[0258] If necessary, the container of disclosed Si-containing film
forming composition may be heated to a temperature that permits the
composition to have a sufficient vapor pressure. The container may
be maintained at temperatures in the range of, for example,
approximately 0.degree. C. to approximately 150.degree. C. Those
skilled in the art recognize that the temperature of the container
may be adjusted in a known manner to control the amount of
composition vaporized.
[0259] For example, the Si-containing film forming compositions may
be introduced into the reactor using the disclosed Si-containing
film forming composition delivery devices. FIGS. 1 and 2 show two
embodiments of the disclosed delivery devices 1.
[0260] FIG. 1 is a side view of one embodiment of the Si-containing
film forming composition delivery device 1. In FIG. 1, the
disclosed Si-containing film forming compositions 10 are contained
within a container 20 having two conduits, an inlet conduit 30 and
an outlet conduit 40. One of ordinary skill in the precursor art
will recognize that the container 20, inlet conduit 30, and outlet
conduit 40 are manufactured to prevent the escape of the gaseous
form of the Si-containing film forming composition 10, even at
elevated temperature and pressure.
[0261] The delivery device should be leak tight and be equipped
with valves that do not permit release of the material. Suitable
valves include spring-loaded or tied diaphragm valves. The valve
may further comprise a restrictive flow orifice (RFO).
[0262] The delivery device may be connected to a gas manifold or in
an enclosure. The gas manifold should permit the safe evacuation
and purging of the piping that may be exposed to air when the
delivery device is replaced so that any residual amounts of the
material do not react. The enclosure may be equipped with sensors
and fire control capability to control the fire in the case of
material release. The gas manifold should also be equipped with
isolation valves, vacuum generators, and permit the introduction of
a purge gas at a minimum.
[0263] The delivery device fluidly connects to other components of
the semiconductor processing tool, such as the gas cabinet
disclosed above, via valves 35 and 45. Preferably, the delivery
device 20, inlet conduit 30, valve 35, outlet conduit 40, and valve
45 are made of 316L EP or 304 stainless steel. However, one of
ordinary skill in the art will recognize that other non-reactive
materials may also be used in the teachings herein and that any
corrosive Si-containing film forming compositions 10 may require
the use of more corrosion-resistant materials, such as Hastelloy or
Inconel.
[0264] In FIG. 1, the end 31 of inlet conduit 30 is located above
the surface of the Si-containing film forming composition 10,
whereas the end 41 of the outlet conduit 40 is located below the
surface of the Si-containing film forming composition 10. In this
embodiment, the Si-containing film forming composition 10 is
preferably in liquid form. An inert gas, including but not limited
to nitrogen, argon, helium, and mixtures thereof, may be introduced
into the inlet conduit 30. The inert gas pressurizes the delivery
device 20 so that the liquid Si-containing film forming composition
10 is forced through the outlet conduit 40 and to components in the
semiconductor processing tool (not shown). The semiconductor
processing tool may include a vaporizer which transforms the liquid
Si-containing film forming composition 10 into a vapor, with or
without the use of a carrier gas such as helium, argon, nitrogen or
mixtures thereof, in order to deliver the vapor to a chamber where
a substrate is located and treatment occurs in the vapor phase.
Alternatively, the liquid Si-containing film forming composition 10
may be delivered directly to the substrate surface as a jet or
aerosol.
[0265] FIG. 2 is a side view of a second embodiment of the
Si-containing film forming composition delivery device 1. In FIG.
2, the end 31 of inlet conduit 30 is located below the surface of
the Si-containing film forming composition 10, whereas the end 41
of the outlet conduit 40 is located above the surface of the
Si-containing film forming composition 10. FIG. 2, also includes an
optional heating element 25, which may increase the temperature of
the Si-containing film forming composition 10. In this embodiment,
the Si-containing film forming composition 10 may be in solid or
liquid form. An inert gas, including but not limited to nitrogen,
argon, helium, and mixtures thereof, is introduced into the inlet
conduit 30. The inert gas bubbles through the Si-containing film
forming composition 10 and carries a mixture of the inert gas and
vaporized Si-containing film forming composition 10 to the outlet
conduit 40 and on to the components in the semiconductor processing
tool.
[0266] Both FIGS. 1 and 2 include valves 35 and 45. One of ordinary
skill in the art will recognize that valves 35 and 45 may be placed
in an open or closed position to allow flow through conduits 30 and
40, respectively. Either delivery device 1 in FIG. 1 or 2, or a
simpler delivery device having a single conduit terminating above
the surface of any solid or liquid present, may be used if the
Si-containing film forming composition 10 is in vapor form or if
sufficient vapor pressure is present above the solid/liquid phase.
In this case, the Si-containing film forming composition 10 is
delivered in vapor form through the conduit 30 or 40 simply by
opening the valve 35 in FIG. 1 or 45 in FIG. 2, respectively. The
delivery device 1 may be maintained at a suitable temperature to
provide sufficient vapor pressure for the Si-containing film
forming composition 10 to be delivered in vapor form, for example
by the use of an optional heating element 25.
[0267] While FIGS. 1 and 2 disclose two embodiments of the
Si-containing film forming composition delivery device 1, one of
ordinary skill in the art will recognize that the inlet conduit 30
and outlet conduit 40 may both be located above or below the
surface of the Si-containing film forming composition 10 without
departing from the disclosure herein. Furthermore, inlet conduit 30
may be a filling port. Finally, one of ordinary skill in the art
will recognize that the disclosed Si-containing film forming
composition may be delivered to semiconductor processing tools
using other delivery devices, such as the ampoules disclosed in WO
2006/059187 to Jurcik et al., without departing from the teachings
herein.
[0268] The vapor of the disclosed Si-containing film forming
compositions is delivered to the reactor of a semiconductor,
photovoltaic, LCD-TFT, flat panel type devices, refractory
materials, or aeronautics tool. The reactor may be any enclosure or
chamber of a device in which vapor deposition methods take place
such as without limitation, a parallel-plate type reactor, a
cold-wall type reactor, a hot-wall type reactor, a single-wafer
reactor, a multi-wafer (i.e., batch) reactor, or other types of
deposition systems suitable to cause the precursor to react and
form the layers. All of these exemplary reactors are capable of
serving as ALD and/or CVD reactors.
[0269] Generally, the reactor contains one or more substrates onto
which the films will be deposited. A substrate is generally defined
as the material on which a process is conducted. The substrates may
be any suitable substrate used in semiconductor, photovoltaic, flat
panel, or LCD-TFT device manufacturing. Examples of suitable
substrates include wafers, such as silicon, silica, glass, or GaAs
wafers. The wafer may have one or more layers of differing
materials deposited on it from a previous manufacturing step. For
example, the wafers may include silicon nitride layers, silicon oxy
nitride layers, carbon doped silicon oxide (SiCOH) layers, tor
combinations thereof. Additionally, the wafers may include copper
layers, tungsten layers, or noble metal layers (e.g. platinum,
palladium, rhodium, or gold). Plastic layers, such as
poly(3,4-ethylenedioxythiophene)poly (styrenesulfonate) [PEDOT:PSS]
may also be used. The layers may be planar or patterned. The
disclosed processes may deposit the silicon-containing layer
directly on the wafer or directly on one or more than one layer
(when patterned layers form the substrate) of the layers on top of
the wafer. Throughout the specification and claims, the wafer and
any associated layers thereon are referred to as substrates. For
example, a Cu film may be deposited onto a SiC layer. In subsequent
processing, a SiC layer may be deposited on the Cu layer, forming a
SiC/Cu/SiC stack used in a damascene structure in the back end of
the line (BEOL).
[0270] The temperature and the pressure within the reactor are held
at conditions suitable for vapor deposition. In other words, after
introduction of the vaporized composition into the chamber,
conditions within the chamber are such that at least part of the
penta-substituted disilane precursor is deposited onto the
substrate to form the silicon-containing film. For instance, the
pressure in the reactor may be held between about 1 Pa and about
10.sup.5 Pa, more preferably between about 25 Pa and about 10.sup.3
Pa, as required per the deposition parameters. Likewise, the
temperature in the reactor may be held between about 100.degree. C.
and about 800.degree. C. One of ordinary skill in the art will
recognize that "at least part of the penta-substituted disilane
precursor is deposited" means that some or all of the precursor
reacts with or adheres to the substrate.
[0271] The temperature of the reactor may be controlled by either
controlling the temperature of the substrate holder or controlling
the temperature of the reactor wall. Devices used to heat the
substrate are known in the art. The reactor wall is heated to a
sufficient temperature to obtain the desired film at a sufficient
growth rate and with desired physical state and composition. A
non-limiting exemplary temperature range to which the reactor wall
may be heated includes from approximately room temperature
(20.degree. C.) to approximately 500.degree. C. When a plasma
deposition process is utilized, the deposition temperature may
range from approximately room temperature (20.degree. C.) to
approximately 400.degree. C. Alternatively, when ozone is used as a
reactant, the deposition temperature may range from approximately
100.degree. C. to approximately 400.degree. C. In another
alternative, when a thermal process is performed, the deposition
temperature may range from approximately 200.degree. C. to
approximately 500.degree. C.
[0272] In addition to the disclosed Si-containing film forming
compositions, a reactant may also be introduced into the reactor.
The reactant may be an oxidizing gas such as one of O.sub.2,
O.sub.3, H.sub.2O, H.sub.2O.sub.2, NO, N.sub.2O, NO.sub.2, oxygen
containing radicals such as O. or OH., NO, NO.sub.2,carboxylic
acids, formic acid, acetic acid, propionic acid, and mixtures
thereof. Typically, the oxidizing gas is selected from the group
consisting of O.sub.2, O.sub.3, H.sub.2O, H.sub.2O.sub.2, oxygen
containing radicals thereof such as O. or OH., and mixtures
thereof. More typically, the oxidizing gas is O.sub.2, O.sub.3,
O.sub.2 plasma, or combinations thereof.
[0273] The reactant may be treated by a plasma, in order to
decompose the reactant into its oxygen containing radical form. For
instance, the plasma may be generated with a power ranging from
about 50 W to about 500 W, preferably from about 100 W to about 200
W. The plasma may be generated or present within the reactor
itself. Alternatively, the plasma may generally be at a location
removed from the reactor, for instance, in a remotely located
plasma system. One of skill in the art will recognize methods and
apparatus suitable for such plasma treatment.
[0274] For example, the reactant may be introduced into a direct
plasma reactor, which generates plasma in the reaction chamber, to
produce the plasma-treated reactant in the reaction chamber.
Exemplary direct plasma reactors include the Titan.TM. PECVD System
produced by Trion Technologies. The reactant may be introduced and
held in the reaction chamber prior to plasma processing.
Alternatively, the plasma processing may occur simultaneously with
the introduction of the reactant. In-situ plasma is typically a
13.56 MHz RF inductively coupled plasma that is generated between
the showerhead and the substrate holder. The substrate or the
showerhead may be the powered electrode depending on whether
positive ion impact occurs. Typical applied powers in in-situ
plasma generators are from approximately 30 W to approximately 1000
W. Preferably, powers from approximately 30 W to approximately 600
W are used in the disclosed methods. More preferably, the powers
range from approximately 100 W to approximately 500 W. The
disassociation of the reactant using in-situ plasma is typically
less than achieved using a remote plasma source for the same power
input and is therefore not as efficient in reactant disassociation
as a remote plasma system, which may be beneficial for the
deposition of Si-containing films on substrates easily damaged by
plasma.
[0275] Alternatively, the plasma-treated reactant may be produced
outside of the reaction chamber. The MKS Instruments' ASTRONi.RTM.
reactive gas generator may be used to treat the reactant prior to
passage into the reaction chamber. Operated at 2.45 GHz, 7 kW
plasma power, and a pressure ranging from approximately 3 Torr to
approximately 10 Torr, the reactant O.sub.2 may be decomposed into
two O. radicals. Preferably, the remote plasma may be generated
with a power ranging from about 1 kW to about 10 kW, more
preferably from about 2.5 kW to about 7.5 kW.
[0276] The resulting silicon oxide films may be used as capacitors
and insulating layers.
[0277] Silicon oxides may be deposited using
pentakis(dimethylamino)disilane and an oxidizing gas in an ALD or
CVD process. The process may be a thermal ALD process at a
temperature ranging from approximately 100.degree. C. to
approximately 400.degree. C. when using an ozone reactant.
Alternatively, the process may be a plasma enhanced ALD process at
a temperature ranging from approximately room temperature
(approximately 23.degree. C.) to 400.degree. C. ALD depositions of
silicon oxide films using the pentakis(dimethylamino)disilane
precursor are expected to produce deposition rates on the order of
approximately 1 angstrom/cycle. Most alkyl amino monosilanes
exhibit a lower deposition rate, typically approximately 0.5
angstroms/cycle.
[0278] As illustrated in the examples, silicon oxide films may also
be deposited at high temperatures using pentachlorodisilane and an
oxidizing gas in an ALD or CVD process. The temperature may range
from approximately 450.degree. C. to approximately 800.degree. C.,
preferably from approximately 450.degree. C. to approximately
600.degree. C., and more preferably from approximately 500.degree.
C. to approximately 600.degree. C. High temperature silicon oxide
film deposition is important to produce films having high density,
low wet etch rates, and low contaminant levels, for example, with
metal impurities ranging from 10.sup.9 to 10.sup.17 atoms/cm.sup.3.
In fact, as shown in Examples 2-5, ALD depositions using
pentachlorodisilane and an ozone/oxygen mixture exhibited
self-limited growth at a temperature range of approximately
550.degree. C. to approximately 650.degree. C. The resulting film
had little to no nitrogen or chlorine contamination. The resulting
silicon oxide film preferably contains between approximately 0
atomic % and approximately 1 atomic % nitrogen. The resulting
silicon oxide film also contains between approximately 0 atomic %
and approximately 1 atomic % chlorine.
[0279] Alternatively, the reactant may be a reducing gas such as
one of H.sub.2, H.sub.2CO, NH.sub.3, SiH.sub.4, Si.sub.2H.sub.6,
Si.sub.3H.sub.8, (CH.sub.3).sub.2SiH.sub.2,
(C.sub.2H.sub.5).sub.2SiH.sub.2, (CH.sub.3)SiH.sub.3,
(C.sub.2H.sub.5)SiH.sub.3, phenyl silane, N.sub.2H.sub.4,
N(SiH.sub.3).sub.3, N(CH.sub.3)H.sub.2, N(C.sub.2H.sub.5)H.sub.2,
N(CH.sub.3).sub.2H, N(C.sub.2H.sub.5).sub.2H, N(CH.sub.3).sub.3,
N(C.sub.2H.sub.5).sub.3, (SiMe.sub.3).sub.2NH,
(CH.sub.3)HNNH.sub.2, (CH.sub.3).sub.2NNH.sub.2, phenyl hydrazine,
N-containing molecules, B.sub.2H.sub.6, 9-borabicyclo[3,3,1]nonane,
dihydrobenzofuran, pyrazoline, trimethylaluminium, dimethylzinc,
diethylzinc, radical species thereof, and mixtures thereof.
Preferably, the reducing as is H.sub.2, NH.sub.3, SiH.sub.4,
Si.sub.2H.sub.6, Si.sub.3H.sub.8, SiH.sub.2Me.sub.2,
SiH.sub.2Et.sub.2, N(SiH.sub.3).sub.3, hydrogen radicals thereof,
or mixtures thereof.
[0280] In another alternative, the reactant may be a
nitrogen-containing reactant such as one of NH.sub.3,
N.sub.2H.sub.4, N(SiH.sub.3).sub.3, N(CH.sub.3)H.sub.2,
N(C.sub.2H.sub.5)H.sub.2, N(CH.sub.3).sub.2H,
N(C.sub.2H.sub.5).sub.2H, N(CH.sub.3).sub.3,
N(C.sub.2H.sub.5).sub.3, (SiMe.sub.3).sub.2NH,
(CH.sub.3)HNNH.sub.2, (CH.sub.3).sub.2NNH.sub.2,
nitrogen-containing radical species thereof, and mixtures
thereof.
[0281] As disclosed above with respect to the oxidizing gas
reactant, the reducing gas or nitrogen containing reactant may also
be treated by a plasma in order to decompose the reactant into its
radical form. N.sub.2 may also be utilized as a reducing gas when
treated with plasma and a blend of N.sub.2 and H.sub.2 may be used
in a remote plasma process. The plasma may be generated in situ or
remotely, as detailed described in further detailed above.
[0282] For example, as illustrated in Examples 7 and 8, silicon
nitride films may be deposited at medium range temperatures using
pentachlorodisilane and a N-containing gas in an ALD or CVD
process. The temperature may range from approximately 350.degree.
C. to approximately 650.degree. C., preferably from approximately
450.degree. C. to approximately 650.degree. C., and more preferably
from approximately 550.degree. C. to approximately 600.degree. C.
This medium range temperature is important to the silicon nitride
deposition process because the underlying substrate may not be able
to withstand higher process temperatures without sustaining damage.
In fact, as shown in Example 8, ALD depositions using
pentachlorodisilane and an ammonia reactant produced silicon
nitride films having a refractive index ranging from approximately
1.7 to approximately 2.2. The refractive index of pure silicon
nitride is 2.0. The incorporation of oxygen or a porous film will
lower the refractive index and an excess of silicon will increase
the refractive index. As shown in Example 8 and FIG. 14, the
resulting film had little to no carbon and traces of oxygen and
chlorine contamination. The silicon nitride film may contain
between approximately 0 atomic % and approximately 5 atomic %
carbon, preferably between approximately 0 atomic % and
approximately 2.5 atomic % carbon; and more preferably between
approximately 0 atomic % and approximately 1 atomic % carbon. The
silicon nitride film may also contain between approximately 0.1
atomic % and approximately 1 atomic % oxygen. Finally, the silicon
nitride film may contain between approximately 0.1 atomic % and
approximately 1 atomic % chlorine.
[0283] The silicon nitride films produced using the disclosed
penta-substituted disilane and nitrogen-containing reactant may be
used as a spacer for a fin double patterning process, as a spacer
for dual Epi sidewall, as a contact etch stop layer, or as a
capping layer for self aligned contacts in FinFET. When used as a
spacer for the fin double patterning process, the silicon nitride
growth rate does not exhibit pattern loading effect (the growth
rate being lower on a dense feature as compared to flat areas of
the substrate). When used as a spacer for a dual Epi sidewall or as
a contact etch stop layer, the silicon nitride film has a low
dielectric constant (between approximately 3 to approximately 6,
preferably between approximately 4.5 and approximately 5.5) and a
low HF wet etch rate (between 0 Ang/sec and 10 Ang/sec for 1% HF at
room temperature).
[0284] The silicon nitride films produced using the disclosed
penta-substituted disilane and nitrogen-containing reactant may
also be used in DRAM manufacturing. More particularly, the silicon
nitride layer may serve as a DRAM spacer, a Buried Word Line (BWL)
nitride cap, a bit line spacer, or a low-k Etch Stop Layer (ESL)
for capacitors.
[0285] The silicon nitride layers produced using the disclosed
penta-substituted disilane and nitrogen-containing reactant may
also be used as a nitride trap layer in 3D NAND manufacturing. The
nitride trap layer should have no seam and a low dielectric
constant (between approximately 3 to approximately 6, preferably
between approximately 4.5 and approximately 5.5).
[0286] The silicon nitride layers produced using the disclosed
penta-substituted disilane and nitrogen-containing reactant may
also be used for encapsulation in MRAM manufacturing. The films
needs to be deposited at low temperature (between approximately
200.degree. C. and approximately 500.degree. C., preferably between
approximately 275.degree. C. and approximately 350.degree. C.) and
should be halide free (containing between approximately 0.1 atomic
% and approximately 1 atomic % halide). PEALD is particularly
suitable for these applications.
[0287] The silicon nitride layers produced using the disclosed
penta-substituted disilane and nitrogen-containing reactant may
also be used as air gap lines in advanced interconnect
manufacturing. The air gap lines need to be deposited at low
temperatures (between approximately 200.degree. C. and
approximately 500.degree. C., preferably between approximately
275.degree. C. and approximately 350.degree. C.), have a low
dielectric constant (between approximately 3 to approximately 6,
preferably between approximately 4.5 and approximately 5.5), have a
low wet etch rate (between 0 Ang/sec and 10 Ang/sec for 1% HF at
room temperature), and be halide free (containing between
approximately 0.1 atomic % and approximately 1 atomic %
halide).
[0288] As shown in Example 10, carbon doped silicon nitrides may
also be deposited using the penta-substituted disilanes, such as
pentakis(dimethylamino)disilane, and a nitrogen containing reactant
in a low temperature plasma enhanced ALD process. Preferably, the
nitrogen containing reactant is NH.sub.3, N.sub.2, or a combination
of N.sub.2 and H.sub.2. The H.sub.2 concentration in the
combination of N.sub.2 and H.sub.2 may range from approximately 0%
vol/vol to approximately 70% vol/vol. For example, the
N.sub.2:H.sub.2 ratio may be 1:1. The process temperature may range
from approximately 100.degree. C. to approximately 350.degree. C.
The carbon concentration in the carbon doped silicon nitride film
may range from approximately 1 atomic % to approximately 15 atomic
%.
[0289] In another alternative, the reactant may be an amine,
alkylaminosilane, or a disilazane to produce a carbon doped silicon
nitride film. Exemplary amines include ammonia. Exemplary
alkylaminosilanes include bis(diethylamino)silane or
tris(dimethylamino)silane. Exemplary disilazanes include
hexamethyldisilazane. The carbon doped silicon nitride film
preferably has a carbon concentration ranging from approximately 2
atomic % to approximately 15 atomic %, a nitrogen concentration
ranging from approximately 10 atomic % to approximately 50 atomic
%, and an oxygen concentration ranging from approximately 0 atomic
% to approximately 5 atomic %.
[0290] In another alternative, the reactant may be an alkyl
substituted metal or metalloid. The alkyl substituted metal or
metalloid may have the formula AlR.sub.3, with each R independently
being H, Me, Et, nPr, iPr, nBu, iBu, or NR2, provided that when
R.sub.3.dbd.H.sub.3 that the molecule may be adducted with an amine
or borohydride. For example, the alkyl substituted metal or
metalloid being triethyl aluminum, trimethyl aluminum, or
AlH.sub.3.NH.sub.3. Alternatively, the alkyl substituted metal or
metalloid may have the formula BR.sub.3, with each R independently
being an alkyl or an allyl group. For example, the alkyl
substituted metal or metalloid may be triethyl boron or trimethyl
boron. Alternatively, the alkyl substituted metal or metalloid may
have the formula AlClR.sub.2, with each R independently being H,
Me, Et, nPr, iPr, nBu, or iBu, or NR.sub.2. In another alternative,
the alkyl substituted metal or metalloid may have the formula
BXR.sub.2, with X being Cl, Br, or I and each R independently being
an alkyl or an allyl group. In yet another alternative, the alkyl
substituted metal or metalloid having the formula ZnR.sub.2, with
each R independently being Me, Et, nPr, iPr, nBu, or iBu. In
another alternative, the alkyl substituted metal or metalloid
having the formula GaR.sub.3, with each R independently being Me,
Et, nPr, iPr, nBu, iBu, or NR.sub.2. For example, the alkyl
substituted metal or metalloid being trimethyl gallium. In yet
another alternative, the alkyl substituted metal or metalloid
having the formula InR.sub.3, with each R independently being Me,
Et, nPr, iPr, nBu, iBu, or NR.sub.2.
[0291] As shown in Example 9, the penta-substituted disilane and
the alkyl substituted metal or metalloid may be used to deposit
silicon carbide films using an ALD process. However, in addition to
the disclosed penta-substituted disilanes, Applicants believe that
any silicon halide precursors may be useful in this process,
provided the precursor contains at least one halide, because the
halide reacts with the metal or metalloid forming a volatile
halide.
[0292] Additional silicon halides that may be suitable for use in
the ALD deposition of silicon carbide films include silicon halides
having the formula SiX.sub.4, each X independently being Cl, Br, I,
H, or R, with R being an aliphatic group. Exemplary silicon halides
include SiCl.sub.3H, SiH.sub.2Cl.sub.2, SiH.sub.3Cl,
SiI.sub.2H.sub.2, SiHMeI.sub.2, or SiMe.sub.2I.sub.2. In another
alternative, the silicon halide may have the formula
Si.sub.2X.sub.6, with each X independently being Cl, Br, I, or H.
Exemplary silicon halides include pentachlorodisilane,
hexachlorodisilane, hexaiododisilane, monochlorodisilane,
monobromodisilane, monoiododisilane, dichlorodisilane
[H.sub.2ClSi--SiCIH.sub.2], dibromodisilane
[H.sub.2BrSi--SiBrH.sub.2], diiododisilane
[H.sub.2ISi--SiIH.sub.2], dichlorodisilane
[H.sub.3Si--SiHCl.sub.2], dibromodisilane [H.sub.3Si--SiHBr.sub.2],
or diiododisilane [H.sub.3Si--SiHI.sub.2]. In another alternative,
the silicon halide may have the formula
X.sub.3Si--CH.sub.2--SiX.sub.3, with each X independently being Cl,
Br, I, or H, such as bis(trichlorosilyl)methane
[Cl.sub.3Si--CH.sub.2--SiCl.sub.3] or bis(dichlorosilyl)methane
[(SiClH.sub.2).sub.2CH.sub.2]. In another alternative, the silicon
halide may have the formula
X.sub.3Si--CH.sub.2--CH.sub.2--SiX.sub.3, with each X independently
being Cl, Br, I, or H, such as
Cl.sub.3Si--CH.sub.2--CH.sub.2--SiCl.sub.3. In another alternative,
the silicon halide may have the formula
X.sub.3Si--CH.sub.2--SiX.sub.2--CH.sub.2--SiX.sub.3, with each X
independently being CI or H, provided at least one terminal X is
Cl. Exemplary silicon halides include
Cl.sub.3Si--CH.sub.2--SiCl.sub.2--CH.sub.2--SiCl.sub.3 or
H.sub.3Si--CH.sub.2--SiH.sub.2--CH.sub.2--SiClH.sub.2. In yet
another alternative, the silicon halide may have the cyclic formula
(--SiX.sub.2--CH.sub.2--).sub.3, with each X independently being
Cl, Br, or I, such as (--SiCl.sub.2--CH.sub.2--).sub.3. In yet
another alternative, the silicon halide may have the cyclic formula
(--SiHX--CH.sub.2--).sub.3, with each X independently being Cl, Br,
or I, such as (--SiHCl--CH.sub.2--).sub.3. The silicon halide may
also be octachlorotrisilane (OCTS or Si.sub.3Cl.sub.8),
decachlorotetrasilane (Si.sub.4Cl.sub.10) or
dodecachloropentasilane (DCPS or Si.sub.5Cl.sub.12). These silicon
halides are either commercially available or may be synthesized by
methods known in the art.
[0293] The vapor deposition conditions within the chamber allow the
disclosed precursor and the reactant to react and form a
silicon-containing film on the substrate. In some embodiments,
Applicants believe that plasma-treating the reactant may provide
the reactant with the energy needed to react with the disclosed
precursor.
[0294] Depending on what type of film is desired to be deposited,
an additional precursor compound may be introduced into the
reactor. The precursor may be used to provide additional elements
to the silicon-containing film. The additional elements may include
lanthanides (Ytterbium, Erbium, Dysprosium, Gadolinium,
Praseodymium, Cerium, Lanthanum, Yttrium), germanium, silicon,
titanium, manganese, ruthenium, bismuth, lead, magnesium, aluminum,
or mixtures of these. When an additional precursor compound is
utilized, the resultant film deposited on the substrate contains
silicon in combination with at least one additional element.
[0295] The Si-containing film forming compositions and reactants
may be introduced into the reactor either simultaneously (chemical
vapor deposition), sequentially (atomic layer deposition) or
different combinations thereof. The reactor may be purged with an
inert gas between the introduction of the composition and the
introduction of the reactant. Alternatively, the reactant and the
composition may be mixed together to form a reactant/composition
mixture, and then introduced to the reactor in mixture form.
Another example is to introduce the reactant continuously and to
introduce the Si-containing film forming composition by pulse
(pulsed chemical vapor deposition).
[0296] The vaporized Si-containing film forming composition and the
reactant may be pulsed sequentially or simultaneously (e.g. pulsed
CVD) into the reactor. Each pulse of the composition may last for a
time period ranging from about 0.01 seconds to about 10 seconds,
alternatively from about 0.3 seconds to about 3 seconds,
alternatively from about 0.5 seconds to about 2 seconds. In another
embodiment, the reactant may also be pulsed into the reactor. In
such embodiments, the pulse of each gas may last for a time period
ranging from about 0.01 seconds to about 10 seconds, alternatively
from about 0.3 seconds to about 3 seconds, alternatively from about
0.5 seconds to about 2 seconds. In another alternative, the
vaporized composition and one or more reactants may be
simultaneously sprayed from a shower head under which a susceptor
holding several wafers is spun (spatial ALD).
[0297] Depending on the particular process parameters, deposition
may take place for a varying length of time. Generally, deposition
may be allowed to continue as long as desired or necessary to
produce a film with the necessary properties. Typical film
thicknesses may vary from several angstroms to several hundreds of
microns, depending on the specific deposition process. The
deposition process may also be performed as many times as necessary
to obtain the desired film.
[0298] In one non-limiting exemplary CVD type process, the vapor
phase of the disclosed Si-containing film forming composition and a
reactant are simultaneously introduced into the reactor. The two
react to form the resulting silicon-containing film. When the
reactant in this exemplary CVD process is treated with a plasma,
the exemplary CVD process becomes an exemplary PECVD process. The
reactant may be treated with plasma prior or subsequent to
introduction into the chamber.
[0299] In one non-limiting exemplary ALD type process, the vapor
phase of the disclosed Si-containing film forming composition is
introduced into the reactor, where it is contacted with a suitable
substrate. Excess composition may then be removed from the reactor
by purging and/or evacuating the reactor. A desired gas (for
example, H.sub.2) is introduced into the reactor where it reacts
with the chemi- or physi-sorbed precursor in a self-limiting
manner. Any excess reducing gas is removed from the reactor by
purging and/or evacuating the reactor. If the desired film is a Si
film, this two-step process may provide the desired film thickness
or may be repeated until a film having the necessary thickness has
been obtained.
[0300] Alternatively, if the desired film contains silicon and a
second element, the two-step process above may be followed by
introduction of the vapor of an additional precursor compound into
the reactor. The additional precursor compound will be selected
based on the nature of the silicon-containing film being deposited.
After introduction into the reactor, the additional precursor
compound is contacted with the substrate. Any excess precursor
compound is removed from the reactor by purging and/or evacuating
the reactor. Once again, a desired gas may be introduced into the
reactor to react with the physi- or chemi-sorbed precursor
compound. Excess gas is removed from the reactor by purging and/or
evacuating the reactor. If a desired film thickness has been
achieved, the process may be terminated. However, if a thicker film
is desired, the entire four-step process may be repeated. By
alternating the provision of the Si-containing film forming
composition, additional precursor compound, and reactant, a film of
desired composition and thickness can be deposited.
[0301] When the reactant in this exemplary ALD process is treated
with a plasma, the exemplary ALD process becomes an exemplary PEALD
process. The reactant may be treated with plasma prior or
subsequent to introduction into the chamber.
[0302] The silicon-containing films resulting from the processes
discussed above may include silicon oxide, silicon nitride, silicon
carbide, and carbon doped silicon nitride films. One of ordinary
skill in the art will recognize that by judicial selection of the
appropriate Si-containing film forming composition, optional
precursor compounds, and reactant species, the desired film
composition may be obtained.
[0303] Upon obtaining a desired film thickness, the film may be
subject to further processing, such as thermal annealing,
furnace-annealing, rapid thermal annealing, UV or e-beam curing,
and/or plasma gas exposure. Those skilled in the art recognize the
systems and methods utilized to perform these additional processing
steps. For example, the silicon-containing film may be exposed to a
temperature ranging from approximately 200.degree. C. and
approximately 1000.degree. C. for a time ranging from approximately
0.1 second to approximately 7200 seconds under an inert atmosphere,
a H-containing atmosphere, a N-containing atmosphere, an
O-containing atmosphere, or combinations thereof. Most preferably,
the temperature is 400.degree. C. for 3600 seconds under a
H-containing atmosphere or an 0-containing atmosphere.
Alternatively, annealing may be performed under a Si-containing
atmosphere, provided the process is performed at a temperature
below the decomposition temperature of the silicon-containing
compound. Exemplary silicon-containing molecules that may be used
to form the silicon-containing atmosphere include SiH.sub.4,
Si.sub.2H.sub.6, MeSiH.sub.3, Me.sub.2SiH.sub.2, aminosilanes,
isocyanato silanes (R--Si--NCO), such as Tetra(isocyanato)silane
(TICS). The resulting film may contain fewer impurities and
therefore may have an improved density resulting in improved
leakage current. The annealing step may be performed in the same
reaction chamber in which the deposition process is performed.
Alternatively, the substrate may be removed from the reaction
chamber, with the annealing/flash annealing process being performed
in a separate apparatus. Any of the above post-treatment methods,
but especially thermal annealing, has been found effective to
densify the films and reduce wet etch rates. This in turn tends to
improve the resistivity of the film.
EXAMPLES
[0304] The following examples illustrate experiments performed in
conjunction with the disclosure herein. The examples are not
intended to be all inclusive and are not intended to limit the
scope of disclosure described herein.
Example 1
Pyrolysis test of Pentachlorodisilane [PCDS or
Si.sub.2HCl.sub.5]
[0305] FIG. 3 is a schematic diagram of deposition apparatus used
for the following testing. The apparatus includes a hotwall tube
reactor 100 containing substrate coupons 105. A pump 110 removes
the contents from the hotwall tube reactor 100.
[0306] The vapor of the disclosed Si-containing film forming
composition is introduced to the hotwall tube reactor 100 from
delivery device 200 via line 201. An inert gas 205, such as
N.sub.2, is delivered to the delivery device 200 via line 206. The
inert gas 205 may also be delivered to the reactor 100 via line
207.
[0307] An oxidizing gas may be introduced to the hotwall tube
reactor 100 from delivery device 300 via line 301. When the
oxidizing gas is ozone, line 301 may include an ozone generator 303
and ozone monitor 304. Oxidizing gas may also be delivered to the
exhaust 311.
[0308] A nitrogen containing gas may be introduced to the hotwall
tube reactor 100 from delivery device 400 via line 401.
[0309] One of ordinary skill in the art will recognize that lines
201, 206, 207, 301, and 401 may include numerous pressure gauges,
check valves, valves, and pressure regulators and that additional
lines for pressure regulation or by-pass flow have not been
included in order to simplify the drawing.
[0310] To examine the thermal decomposition behavior of PCDS,
pyrolysis testing was performed in the deposition apparatus of FIG.
3 at 4 different temperatures (400, 500, 600 and 700.degree. C.)
for 30 min on a SiO.sub.2 substrate or coupon. The hot wall tube
reactor was kept at 1 Torr, with 4 sccm of a continuous flow of
PCDS into the reaction chamber using 50 sccm of N.sub.2 as a
carrier gas. Pyrolysis mimics chemical vapor deposition without a
reactant and illustrates the temperature at which the precursor
self decomposes.
[0311] FIGS. 4(a), (b), (c), and (d) are X-ray Photoelectron
Spectroscopy (XPS) depth profiles of the resulting Si films. As can
be seen in FIGS. 4(a) and (b), no thermal decomposition of PCDS
occurred because no silicon layers were formed, with the testing
revealing the original SiO.sub.2 substrate. FIG. 4(c) reveals
partial decomposition of the PCDS resulting in a Si-rich SiO.sub.2
layer at 600.degree. C. As can be seen in FIG. 4(d), an almost 100%
Si layer having little to no O, Cl or C inclusion was formed on the
SiO.sub.2 substrate from decomposition of PCDS alone at
600.about.700.degree. C.
Comparative Example 1
Pyrolysis test of Hexachlorodisilane [HCDS or Si.sub.2Cl.sub.6]
[0312] Comparative pyrolysis testing of hexachlorodisilane (HCDS or
Si.sub.2Cl.sub.6) was performed at 4 different temperatures (400,
500, 600 and 700.degree. C.) for 30 min on a SiO.sub.2 substrate in
the deposition apparatus of FIG. 3. The hot wall tube reactor was
kept at 1 Torr, with 4 sccm of a continuous flow of HCDS into the
reaction chamber using 50 sccm of N.sub.2 as a carrier gas.
[0313] FIGS. 5(a), (b), (c), and (d) show X-ray Photoelectron
Spectroscopy (XPS) depth profiles of the resulting Si-containing
films. As can be seen, no pure Si layers were formed by HCDS
decomposition at any temperature.
Example 2
SiO.sub.2 ALD using PCDS or HCDS and O.sub.3/O.sub.2
[0314] SiO.sub.2 ALD was performed using PCDS with O.sub.3 as an
oxidizing agent at the temperature range of 500.about.700.degree.
C. on Si substrates. The reaction furnace of FIG. 3 was controlled
at 1 Torr and 50 sccm of N.sub.2 was continuously flowed. The ALD
process included the following steps: 1) supply a pulse of 4 sccm
of PCDS to the reaction chamber for 10 seconds, 2) purge the excess
precursors by 50 sccm of N.sub.2 for 90 seconds, 3) supply
.about.7.2% of O.sub.3/O.sub.2 (O.sub.2: 100 sccm) to the chamber
for 10 seconds, 4) purge excess O.sub.3/O.sub.2 by 50 sccm of
N.sub.2 for 30 seconds. The sequence from 1) to 4) was repeated for
200 cycles, until the deposited layer achieved suitable thickness
for film characterization (i.e., over 100 .ANG.). The method was
repeated with HCDS replacing PCDS with the same ALD process
conditions as PCDS. The average deposition rates from 4 separate
coupon substrate locations using PCDS (circle) and 4 separate
coupon locations using HCDS (triangle) are shown in FIG. 6.
[0315] The deposition rate of PCDS increased from 500.degree. C. to
600.degree. C., and exhibited a plateau between 600.degree. C. and
650.degree. C., then increased again up to 700.degree. C. From this
temperature dependency of deposition rate of PCDS in ALD process,
an ALD window may be observed between 600.degree. C. and
650.degree. C. However in the same Figure, the deposition rate of
HCDS continuously increased in the temperature range of 500.degree.
C. to 700.degree. C. As a result, no considerable ALD window was
observed for HCDS. Applicants believe that the SiO.sub.2 ALD window
(i.e., 600-650.degree. C.) obtained from PCDS provides the highest
temperature ALD window using a chlorosilane based Si precursors,
like monochlorosilane or hexachlorodisilane. One of ordinary skill
in the art will recognize that temperature and pressure may be
manipulated to change this ALD deposition window.
Example 3
SiO.sub.2 ALD Saturation Behavior of PCDS and O.sub.3
[0316] Based on the results from Example 2, the PCDS pulse time
dependency of SiO.sub.2ALD growth behaviour is examined at two
temperatures, 550.degree. C. and 600.degree. C., and the result is
provided in FIG. 7. The same process conditions used for the
temperature dependency test in Example 2 were applied to this
evaluation, except the pulse time of PCDS was varied at both
550.degree. C. (diamond) and 600.degree. C. (square). At both
temperatures, stable average deposition rates are observed with
pulse times of PCDS between 10-15 seconds from 3-5 locations on the
coupon: 0.91.about.0.94 .ANG./cycle at 600.degree. C. and
0.50.about.0.52 .ANG./cycle at 550.degree. C. The consistent
deposition rates are considered a characteristic of ALD
saturation.
Example 4
SiO.sub.2 ALD Film Composition by XPS
[0317] XPS analysis was performed for SiO.sub.2 ALD films deposited
in Example 2 from PCDS on Si substrates at 550, 600, 650, and
700.degree. C. to examine the film composition. FIGS. 8a-d shows
the result of XPS depth profile of 5-elements, Si, Cl, C, N and O.
No Cl, C and N was detected in the films. The XPS sputter energy
was set higher for the films deposited at 650.degree. and
700.degree. C. than for those deposited at 550.degree. C. and
600.degree. C. As a result, the analysis results for the etch times
of the films deposited at 650.degree. and 700.degree. C. penetrates
deeper into the films than equivalent etch times of the films
deposited at 550.degree. C. and 600.degree. C.
Example 5
Step Coverage of SiO.sub.2 ALD Film Using PCDS
[0318] Step coverage of SiO.sub.2 films deposited by ALD was
examined on pattern wafers with holes having an aspect ratio
(AR)=40 with a 8 micrometer depth at 600.degree. C. The reaction
furnace of FIG. 3 was controlled at 1 Torr and 50 sccm of N.sub.2
was continuously flowed. The ALD process included the following
steps: 1) supply a pulse of 4 sccm of PCDS to the reaction chamber
for 10 seconds, 2) purge the excess precursors by 50 sccm of
N.sub.2 for 90 seconds, 3) supply .about.7.2% of O.sub.3/O.sub.2
(O2: 100 sccm) to the chamber for 10 seconds, 4) purge excess
O.sub.3/O.sub.2 by 50 sccm of N.sub.2 for 10 seconds. The sequence
from 1) to 4) was repeated for 350 cycles. FIGS. 9 and 9(a)-(c) are
scanning electron microscope pictures showing the resulting step
coverage in the entire hole (FIG. 9) and three different positions
within FIG. 9: (FIG. 9(a)) top step coverage=93%, (FIG. 9(b))
middle (around 2 micrometer depth from top) step coverage=77% and
(FIG. 9(c)) bottom step coverage=73%.
Example 6
Catalytic Low Temperature SiO.sub.2 ALD
[0319] SiO.sub.2 films were deposited using ALD with PCDS, H.sub.2O
as an oxidizing agent, and triethylamine (TEA) as a catalyst. The
reaction furnace of FIG. 3 was controlled at 5 Torr, at the
temperature range of 50.about.100.degree. C., and 200 sccm of Ar
was continuously flowed. The deposition process included the
following steps: 1) introducing a pulse of 1 sccm of PCDS and 50
sccm of TEA to the reaction furnace for 10 seconds, 2) purging
excess PCDS and TEA from the reaction furnace by 1 slm of Ar for 10
seconds, 3) introducing 15 sccm of H.sub.2O and 50 sccm of TEA and
1 slm of Ar to the furnace for 20 seconds, 4) purging excess
H.sub.2O and TEA by 1 slm of Ar for 20 seconds. The sequence from
1) to 4) was repeated for 300 cycles.
[0320] FIG. 10 is a graph demonstrating the process temperature
dependence of deposition rate (hollow diamond) and refractive index
(solid square). Deposition rates of .about.1.4 .ANG./cycle and
refractive index of .about.1.39 was obtained at 70.degree. C.,
indicating a low density film that may be suitable for sacrificial
use. FIG. 11 is a graph demonstrating the XPS depth profile of the
deposited SiO.sub.2 film at 70.degree. C., which demonstrates that
the resulting film contains no impurities.
Example 7
Low Temperature CVD of SiN
[0321] SiN films were deposited via CVD using PCDS (circle) or HCDS
(square) as a Si source and ammonia (NH.sub.3) as a nitridation
source. The reaction furnace of FIG. 3 was controlled at 1 Torr,
temperature varied from 450.degree. C. to 600.degree. C., and 100
sccm of Ar was continuously flowed. A mixed gas flow of 1 sccm of
Si source and 25 sccm of NH.sub.3 was supplied to the reaction
furnace for 60.about.120 minutes, until the deposited layer
achieved suitable thickness. FIG. 12 is a graph illustrating the
deposition rate (hollow) and refractive index (solid) obtained with
PCDS+NH.sub.3 than that with HCDS+NH.sub.3.
Example 8
Medium Temperature ALD of SiN
[0322] SiN films were deposited via ALD using PCDS (circle), HCDS
(square), or OCTS (octachlorotrisilane)(triangle) as a Si source
and ammonia (NH.sub.3) as a nitridation source. The pressure in the
reaction furnace of FIG. 3 is controlled at 5 Torr, the temperature
varied from 350.degree. C. to 600.degree. C., and 100 sccm of Ar
was continuously flowing. The deposition process includes the
following steps: 1) introducing a pulse of 1 sccm of Si source to
the reaction furnace for 10 seconds, 2) purging excess Si source
from the reaction furnace by 1 slm of Ar for 10 seconds, 3)
introducing 50 sccm of NH.sub.3 to the reaction furnace, and 4)
purging excess NH.sub.3 from the reaction furnace by 1 slm of Ar
for 20 seconds. The sequence from 1) to 4) were repeated for
200.about.400 cycles, until the deposited layer achieved suitable
thickness of over 100 .ANG..
[0323] FIG. 13 is a graph demonstrating the temperature dependence
of the PCDS (circle), HCDS (square), and OCTS (triangle) deposition
rates (hollow) and refractive indices (solid) from the process.
[0324] PCDS exhibited higher deposition rates and refractive
indices as compared to HCDS or OCTS, except the refractive index
value of HCDS is higher at 400.degree. C. and 550.degree. C. The
deposition rate of PCDS and HCDS exhibit a plateau between
550.degree. C. and 600.degree. C., indicating self-limiting ALD
behavior, but no plateau was observed from OCTS.
[0325] FIG. 14 is a graph demonstrating the XPS depth profile of
the SiN film deposited at 600.degree. C. with PCDS and NH.sub.3,
including the 54% of Si, 45% of N, and trace amount of 0, C, and Cl
impurities.
[0326] As shown in FIG. 13, silicon nitride films with refractive
indices that may be acceptable for use in the fabrication of
semiconductor devices are deposited at substrate temperatures
ranging from 450.degree. C. to 600.degree. C. using PCDS and
ranging from 500.degree. C. to 600.degree. C. using HCDS. The
refractive index of silicon nitride films deposited from OCTS only
become commercially viable at 600.degree. C. Furthermore, the
deposition rate of silicon nitride films from PCDS is substantially
higher than from HCDS within this temperature range (i.e., 40%-100%
higher). Using PCDS therefore allows formation of a high quality
silicon nitride film at a lower temperature and with a surprisingly
high deposition rate. The temperature range extension producing
refractive indices near that of pure silicon nitride for PCDS as
compared to HCDS is also surprising and beneficial for producing
semiconductor devices. A desired silicon nitride film may be
obtained at substrate temperatures 50.degree. C. lower than was
possible using the industry standard material HCDS. The lower
temperature permits a lower thermal budget in processing which
allows for more flexibility and options for subsequent processing
steps.
Example 9
Low Temperature ALD of SiC
[0327] SiC films were deposited via ALD using PCDS (square) or HCDS
(triangle) as a Si source and trimethylalumimum (TMA) as a carbon
source. The pressure in the reaction furnace of FIG. 3 was
controlled at 8 Torr, the temperature varied from 350.degree. C. to
400.degree. C., and 10 sccm of N.sub.2 was continuously flowing.
The deposition process includes the following steps: 1) introducing
a pulse of 0.8 sccm of Si source to the reaction furnace for 15
seconds, 2) purging excess Si source from the reaction furnace by
25 sccm of N.sub.2 for 30 seconds, 3) introducing 1.8 sccm of TMA
to the reaction furnace, and 4) purging excess TMA from the
reaction furnace by 25 sccm of N.sub.2 for 60 seconds. The sequence
from 1) to 4) was repeated 290 cycles, until the deposited layer
achieved suitable layer thickness of over 100 .ANG.. FIG. 15 shows
the XPS depth profile of the SiC films deposited at 400.degree. C.,
including the O, Al, Cl impurities. FIG. 16 shows the film
thickness (hollow) and refractive indices (solid) based on the
measurement position. The graph illustrates the higher refractive
index obtained with PCDS+TMA than that with HCDS +TMA. The films
having the higher refractive index (i.e., from PCDS+TMA) may be
more dense than those with the lower refractive index (i.e., from
HCDS+TMA), which may enhance wet etching resistivity.
Example 10
Low-T PEALD of Si(C)N
[0328] FIG. 17 is a schematic diagram of deposition apparatus used
for the testing of Example 10. The apparatus includes a reactor 100
containing a wafer stage 101. The wafer is transferred to the wafer
stage 101 by load lock chamber 102, which is connected to pump 108.
A showerhead 103 is located in the top of the reactor 100, and
plasma may be generated by the RF generator 106. A dry pump 105
removes the contents of the reactor 100.
[0329] The disclosed Si-containing precursor is introduced to the
reactor 100 from delivery device 200 via line 201. An inert gas
300, such as Ar, is delivered to the delivery device 200 via line
301. The inert gas 300 may also be delivered to the reactor 100 via
line 302.
[0330] A nitridation gas 400, such as N.sub.2, is introduced to the
reactor 100 via line 401. The inert gas 300 may also be delivered
to the nitridition gas 400 via line 303.
[0331] One of ordinary skill in the art will recognize that lines
201, 301, 302, 303, and 401 may include numerous pressure gauges,
check valves, valves, and pressure regulators and that additional
lines for pressure regulation or by-pass flow have not been
included in order to simplify the drawing.
[0332] Si(C)N films were deposited at low temperature using
pentakis (dimethylamino) disilane (Si.sub.2H(NMe.sub.2).sub.5) as a
Si source and a nitrogen containing reactant via a plasma enhance
ALD process using the deposition apparatus of FIG. 17. The process
was done on 6'' Si wafer, under direct plasma mode. The pressure in
the reaction furnace of FIG. 17 is controlled at 1 Torr, the
temperature varied from 200.degree. C. to 400.degree. C., and 500
sccm of Ar was continuously flowing. The deposition process
includes the following steps: 1) introducing a N.sub.2 plasma pulse
(100 W) of 100 sccm of N.sub.2 to the reaction furnace for 7
seconds, 2) purging the reaction furnace by 500 sccm of N.sub.2 for
3 seconds, 3) introducing 1 sccm of Pentakis(dimethylamino)disilane
to the reaction furnace for 5 seconds, and 4) purging excess Si
precursor from the reaction furnace by 500 sccm of N.sub.2 for 5
seconds. The sequence from 1) to 4) was repeated 500 cycles until
the deposited layer achieved suitable layer thickness of over 100
.ANG..
[0333] FIG. 18 shows the XPS depth profile of the Si(C)N film
deposited at 275.degree. C., which exhibited a formation of SiN,
with .about.11% C and .about.2% O in the film. FIG. 19 shows the Si
exposure time of deposition rate (square) and refractive index
(circle) at a 10 second (solid) and 20 second (hollow) purge time.
The graph, in case of 10 sec purge time, illustrates that the
deposition rate increased corresponding to Si exposure time, but
the refractive index remained stable at 1.8 to Si exposure time.
However when the Si purge time increased from 10 sec to 20 sec, for
the case of 20 sec Si exposure time, the deposition rate decreased
from 0.5 .ANG./cycle to 0.42 .ANG./cycle, and the RI increased from
1.78 to 1.81, which may demonstrate an inefficient purge time for
the longer pulse process.
[0334] It will be understood that many additional changes in the
details, materials, steps, and arrangement of parts, which have
been herein described and illustrated in order to explain the
nature of the invention, may be made by those skilled in the art
within the principle and scope of the invention as expressed in the
appended claims. Thus, the present invention is not intended to be
limited to the specific embodiments in the examples given above
and/or the attached drawings.
* * * * *